WO2024214743A1 - Dihydroxybiphenyl compound, bisphosphite compound, catalyst, catalyst composition, method for producing aldehyde, and method for producing alcohol - Google Patents

Abstract

Disclosed is a dihydroxybiphenyl compound which is represented by general formula (1). (In the formula, X represents an alkylene group having 4 to 20 carbon atoms. R1, R11, R3 and R13 each represent a tertiary alkyl group having 4 to 7 carbon atoms, or the like, and preferably represent a t-butyl group. R2 and R12 each represent a hydrogen atom or the like. R4 and R14 each represent an alkyl group having 1 to 3 carbon atoms, or the like, and preferably represent a methyl group. R1 and X-R11 are different from each other.)

Description

Dihydroxybiphenyl compound, bisphosphite compound, catalyst, catalyst composition, method for producing aldehyde, and method for producing alcohol

The present invention relates to a novel dihydroxybiphenyl compound and a novel bisphosphite compound which is a derivative thereof.
Furthermore, the present invention relates to catalysts and catalyst compositions containing said bisphosphite compounds.
Furthermore, the present invention relates to a method for producing an aldehyde and a method for producing an alcohol using the bisphosphite compound or the catalyst.

The method of producing aldehydes or their hydrogenated products, alcohols, by reacting olefinic compounds with synthesis gas (a mixture of carbon monoxide and hydrogen) in the presence of a catalyst is known as the hydroformylation method (reaction). Catalysts used in hydroformylation reactions are usually soluble complexes of long-form Group 8 metals in the periodic table with organophosphorus compounds as ligands.

　In general, the ligands used together with the metal component of the catalyst have a significant effect on the catalytic reaction. It is widely known that the activity and selectivity of the hydroformylation reaction also vary greatly depending on the ligands. To carry out the hydroformylation reaction industrially and profitably, it is important to improve the selectivity of linear aldehyde isomers while maintaining good reaction activity, and the design of ligands for this purpose is being actively pursued.

Various phosphite compounds are known as a group of phosphorus compounds used as ligands in hydroformylation reactions. In addition to simple monophosphites such as trialkyl phosphites and triaryl phosphites, polyphosphites that have multiple coordinating phosphorus atoms in the molecule have been proposed as various phosphite compounds.

In recent years, bisphosphite compounds have been reported as polyphosphite compounds having multiple coordinating phosphorus atoms in the molecule, which have bulky substituents in the ring structure and are made from dihydroxybiphenyl compounds having an asymmetric structure (Patent Document 1). Such bisphosphite compounds are known to provide extremely excellent selectivity for linear aldehyde isomers in hydroformylation reactions.

　With this background technology in mind, if a novel dihydroxybiphenyl compound having a bulky substituent in the ring structure and an asymmetric structure can be obtained, it is expected that a catalyst using a bisphosphite compound made from the dihydroxybiphenyl compound as a ligand together with a metal component will provide extremely excellent selectivity for linear aldehyde isomers in hydroformylation reactions.

International Publication No. 2019/039565

The present invention has been made in consideration of the problems of the conventional technology described above, and aims to provide a novel dihydroxybiphenyl compound that has a bulky substituent in the ring structure, has an asymmetric structure, and can be used as a raw material for a bisphosphite compound that provides excellent linear aldehyde isomer selectivity in the hydroformylation reaction of an olefin compound.

A further object of the present invention is to provide a novel bisphosphite compound which, in the hydroformylation reaction of an olefin compound, gives an extremely excellent selectivity for a straight-chain aldehyde isomer and which is produced from the above-mentioned novel bisphosphite compound as a raw material.
A further object of the present invention is to provide a catalyst and a catalyst composition containing the bisphosphite compound.
A further object of the present invention is to provide a method for producing an aldehyde, which comprises reacting an olefin compound with carbon monoxide and hydrogen using the bisphosphite compound or the catalyst to obtain an aldehyde.
A further object of the present invention is to provide a method for producing an alcohol, comprising producing an alcohol by using the aldehyde obtained by the method for producing an aldehyde.

As a result of extensive research aimed at solving the above problems, the inventors have succeeded in synthesizing a novel dihydroxybiphenyl compound and completed the present invention. That is, the gist of the present invention is as follows:

[1] A dihydroxybiphenyl compound represented by the following general formula (1):

(In formula (1),
X is an alkylene group having 4 to 20 carbon atoms;
R ¹ and R ¹¹ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, and a cycloalkyl group having 3 to 20 carbon atoms, and R ¹ and X-R ¹¹ are different from each other.
R ² and R ¹² each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, an alkoxy group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, a cycloalkoxy group having 3 to 20 carbon atoms, a dialkylamino group having 2 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an aryloxy group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, an alkylaryloxy group having 7 to 20 carbon atoms, an arylalkyl group having 7 to 20 carbon atoms, an arylalkoxy group having 7 to 20 carbon atoms, a cyano group, a hydroxyl group, and a halogen atom;
R ³ and R ¹³ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, and an arylalkyl group having 7 to 20 carbon atoms;
^R4 and ^R14 each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms, an alkoxy group having 1 to 12 carbon atoms, a silyl group, a siloxy group, and a halogen atom.

[2] The dihydroxybiphenyl compound according to [1], wherein in the general formula (1), X is an alkylene group having 4 to 20 carbon atoms, including a quaternary carbon atom.

[3] The dihydroxybiphenyl compound according to [2], wherein X is an alkylene group having 4 to 5 carbon atoms including a quaternary carbon atom.

[4] The dihydroxybiphenyl compound according to [3], wherein X is an alkylene group having a structural unit represented by the following formula (1X):
-C(CH ₃ ) ₂ -CH ₂ - (1X)

[5] The R ¹ and R ¹¹ are each independently a tertiary alkyl group having 4 to 20 carbon atoms;
^R2 and ^R12 are hydrogen atoms,
R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 20 carbon atoms;
The dihydroxybiphenyl compound according to any one of [1] to [4], wherein R ⁴ and R ¹⁴ are each independently selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, an alkoxy group having 1 to 3 carbon atoms, and a halogen atom.

[6] The R ¹ , R ¹¹ , R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 7 carbon atoms;
The dihydroxybiphenyl compound according to [5], wherein R ⁴ and R ¹⁴ are each independently an alkyl group having 1 to 3 carbon atoms.

[7] The dihydroxybiphenyl compound according to [6], wherein R ¹ , R ¹¹ , R ³ and R ¹³ are t-butyl groups, and R ⁴ and R ¹⁴ are methyl groups.

[8] A bisphosphite compound represented by the following general formula (2):

(In formula (2),
X is an alkylene group having 4 to 20 carbon atoms;
R ¹ and R ¹¹ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, and a cycloalkyl group having 3 to 20 carbon atoms, and R ¹ and X-R ¹¹ are different from each other.
R ² and R ¹² each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, an alkoxy group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, a cycloalkoxy group having 3 to 20 carbon atoms, a dialkylamino group having 2 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an aryloxy group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, an alkylaryloxy group having 7 to 20 carbon atoms, an arylalkyl group having 7 to 20 carbon atoms, an arylalkoxy group having 7 to 20 carbon atoms, a cyano group, a hydroxyl group, and a halogen atom;
R ³ and R ¹³ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, and an arylalkyl group having 7 to 20 carbon atoms;
^R4 and ^R14 each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms, an alkoxy group having 1 to 12 carbon atoms, a silyl group, a siloxy group, and a halogen atom.
Z ¹ to Z ⁴ each independently represent an aryl group having 6 to 20 carbon atoms, and may have a substituent, and the substituents may be bonded to each other to form a ^ring .
and Z ² , and Z ³ and Z ⁴ may not be bonded to each other, or may be bonded to each other to form a ring structure.

[9] The bisphosphite compound according to [8], wherein X is an alkylene group having 4 to 20 carbon atoms, including a quaternary carbon atom.

[10] The bisphosphite compound according to [9], wherein X is an alkylene group having 4 to 5 carbon atoms including a quaternary carbon atom.

[11] The bisphosphite compound according to [10], wherein X is an alkylene group having a structural unit represented by the following formula (1X):
-C( _CH3 ) ₂ - _CH2- (1X)

[12] The R ¹ and R ¹¹ are each independently a tertiary alkyl group having 4 to 20 carbon atoms;
R ² and R ¹² are hydrogen atoms, R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 20 carbon atoms,
The bisphosphite compound according to any one of [8] to [11], wherein R ⁴ and R ¹⁴ are each independently selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, an alkoxy group having 1 to 3 carbon atoms, and a halogen atom.

[13] The bisphosphite compound according to any one of [8] to [12], wherein Z ¹ to Z ⁴ each independently have no substituent on an aromatic ring carbon atom adjacent to a carbon atom bonded to an oxygen atom, or have a substituent having 0 to 2 carbon atoms on the aromatic ring carbon atom.

[14] The R ¹ , R ¹¹ , R ³ and R ¹³ each independently represent a tertiary alkyl group having 4 to 7 carbon atoms;
The bisphosphite compound according to [12] or [13], wherein R ⁴ and R ¹⁴ are each independently an alkyl group having 1 to 3 carbon atoms.

[15] The bisphosphite compound according to any one of [8] to [14], wherein Z ¹ to Z ⁴ are each independently a 1-naphthyl group or a 2-naphthyl group.

[16] The bisphosphite compound according to [14] or [15], wherein R ¹ , R ¹¹ , R ³ and R ¹³ are t-butyl groups, and R ⁴ and R ¹⁴ are methyl groups.

[17] A catalyst comprising a complex of a bisphosphite compound according to any one of [8] to [16] and a metal of Groups 8 to 10.

[18] The catalyst according to [17], in which the molar ratio of the bisphosphite compound to the Group 8 to 10 metal is 0.00004 to 500.

[19] The catalyst according to [18], in which the molar ratio of the bisphosphite compound to the Group 8 to 10 metal is 0.0002 to 100.

[20] The catalyst according to [19], in which the molar ratio of the bisphosphite compound to the Group 8 to 10 metal is 0.001 to 50.

[21] A catalyst composition comprising a bisphosphite compound represented by the following general formula (3) and a bisphosphite compound according to any one of [8] to [16].

(In formula (3),
R ¹ , R ² and R ¹² , R ³ and R ¹³ , R ⁴ and R ¹⁴ , and Z ¹ to Z ⁴ are respectively defined as R ¹ , R ² and R ¹² , R ³ and R ¹³ , R ⁴ and R ¹⁴ , and Z ¹ to Z ⁴ in the general formula (2).

[22] The catalyst composition according to [21], in which the content of the bisphosphite compound represented by the general formula (3) is 80.0 mass% or more, and the content of the bisphosphite compound according to any one of [8] to [16] is 0.01 mass% or more.

[23] A method for producing an aldehyde by reacting an olefin compound with carbon monoxide and hydrogen in the presence of a Group 8 to 10 metal compound and a bisphosphite compound according to any one of [8] to [16].

[24] The method for producing an aldehyde according to [23], wherein the concentration of the Group 8 to 10 metal compound in the reaction solution is 0.05 to 5000 mg/L in terms of metal atoms.

[25] A method for producing an alcohol by producing an aldehyde by the method for producing an aldehyde described in [23] or [24], and then reacting the aldehyde with hydrogen.

[26] A method for producing an aldehyde by reacting an olefin compound with carbon monoxide and hydrogen in the presence of a catalyst according to any one of [17] to [20].

[27] A method for producing an alcohol by producing an aldehyde by the method for producing an aldehyde described in [26] and then reacting the aldehyde with hydrogen.

The present invention provides a novel dihydroxybiphenyl compound that has a bulky substituent in the ring structure, has an asymmetric structure, and can be used as a bisphosphite compound that provides extremely excellent linear aldehyde isomer selectivity in the hydroformylation reaction of olefin compounds.

The catalyst and catalyst composition using the bisphosphite compound of the present invention, which is made from the dihydroxybiphenyl compound of the present invention as a raw material, as a ligand together with a metal component, can obtain extremely excellent selectivity for linear aldehyde isomers while maintaining good reaction activity in the hydroformylation reaction of olefin compounds.
Therefore, according to the present invention, it is possible to provide a bisphosphite compound which can provide extremely excellent selectivity for a straight-chain aldehyde isomer in the hydroformylation reaction of an olefin compound.

Furthermore, according to the present invention, there can be provided a method for producing an aldehyde, which comprises reacting an olefin compound with carbon monoxide and hydrogen using the bisphosphite compound or the catalyst to obtain an aldehyde with excellent linear aldehyde isomer selectivity.
Furthermore, according to the present invention, there can be provided a method for producing an alcohol, which comprises using the aldehyde obtained by the method for producing an aldehyde.

Fig. 1(a) is a ¹ H-NMR spectrum of the compound A produced in Experimental Example 1. Fig. 1(b) is a ¹³ C-NMR spectrum of the compound A. Fig. 2(a) is a ¹ H-NMR spectrum of the compound B produced in Experimental Example 2. Fig. 2(b) is a ¹³ C-NMR spectrum of the compound B.

The following describes in detail an embodiment of the present invention. The present invention is not limited to the following description, and can be modified as desired without departing from the spirit of the present invention.

In this specification, unless otherwise specified, a numerical range expressed using "~" means a range that includes the numerical values written before and after "~" as the lower and upper limits. "A~B" means greater than or equal to A and less than or equal to B.

In this specification, "including A or B" means "including A," "including B," and "including A and B," unless otherwise specified.

In this specification, "GC area %" refers to the composition ratio of each component measured using a gas chromatogram (GC) measuring device and a gas chromatography total area method, and is calculated as the area content ratio (unit: GC area %) of each peak component when the total area of the GC peaks of all products on the gas chromatogram is taken as 100%. Details of the GC measurement conditions will be explained in the experimental examples described later.
In this specification, "LC area %" refers to the composition ratio of each component measured using a liquid chromatogram (LC) measuring device and a liquid chromatography (LC method) total area method, and is calculated as the area content ratio (unit: LC area %) of each peak component when the total area of the LC peaks of all products on the liquid chromatogram is taken as 100%. Details of the LC measurement conditions will be explained in the experimental examples described later.

In this specification, "mass %" indicates the content ratio of a specific component contained in a total amount of 100 mass %. Moreover, "mass %" and "weight %" have the same meaning.
As used herein, "optional" or "optionally" means that the subsequently described situation may or may not occur, and thus the description includes both the occurrence and non-occurrence of the situation.

As used herein, the term "about" can mean 20% above or below the stated value. For example, a temperature of about 75°C relative to 0°C Celsius encompasses the range of 60°C to 90°C.
All steps described herein can be performed in any suitable order unless otherwise indicated herein or clearly contradicted by context.

The following is a detailed description of an embodiment of the present invention. The following description of the components is an example of an embodiment of the present invention, and the present invention is not limited to these contents.

Hereinafter, "a catalyst using a bisphosphite compound made from the dihydroxybiphenyl compound of the present invention as a ligand together with a metal component has excellent linear aldehyde isomer selectivity in a hydroformylation reaction" may be abbreviated to simply "has excellent aldehyde isomer selectivity."

[Dihydroxybiphenyl compounds]
The dihydroxybiphenyl compounds of the present invention are novel dihydroxybiphenyl compounds each represented by the following general formula (1).

(In formula (1),
X is an alkylene group having 4 to 20 carbon atoms;
R ¹ and R ¹¹ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, and a cycloalkyl group having 3 to 20 carbon atoms, and R ¹ and X-R ¹¹ are different from each other.
R ² and R ¹² each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, an alkoxy group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, a cycloalkoxy group having 3 to 20 carbon atoms, a dialkylamino group having 2 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an aryloxy group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, an alkylaryloxy group having 7 to 20 carbon atoms, an arylalkyl group having 7 to 20 carbon atoms, an arylalkoxy group having 7 to 20 carbon atoms, a cyano group, a hydroxyl group, and a halogen atom;
R ³ and R ¹³ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, and an arylalkyl group having 7 to 20 carbon atoms;
^R4 and ^R14 each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms, an alkoxy group having 1 to 12 carbon atoms, a silyl group, a siloxy group, and a halogen atom.

<Structural features>
As shown in the above general formula (1), the dihydroxybiphenyl compound of the present invention has a biphenyl skeleton in the molecule and different substituents, -R ¹ and -X-R ¹¹ , at the 5-position and 5'-position of the biphenyl skeleton (ortho positions relative to the hydroxyl groups substituted at the 6-position and 6'-position), giving it an asymmetric structure. In addition, the dihydroxybiphenyl compound has a structural feature in which one of the substituents, -X-R ¹¹ , is a bulky substituent.
Since the dihydroxybiphenyl compound of the present invention has such structural features, it can provide the following effects.
(1) The asymmetric structure and bulky substituent (-X-R ¹¹ ) provide a stabilizing effect against hydrolysis to the bisphosphite compound of the present invention, which is to be described later and which is synthesized using the dihydroxybiphenyl compound as a precursor.
(2) This asymmetric structure and the bulky substituent (-X-R ¹¹ ) provide a stabilizing effect against hydrolysis even in the catalyst using the bisphosphite compound, and the bulky substituent (-X-R ¹¹ ) controls the coordination direction when the olefin compound coordinates to a metal, thereby providing extremely excellent selectivity for straight-chain aldehyde isomers.

＜X＞
In general formula (1), X is an alkylene group having 4 to 20 carbon atoms.
Preferably, X is an alkylene group having from 4 to 20 carbon atoms, including a quaternary carbon atom.
In the present invention, a quaternary carbon atom means a carbon atom in which all of the bonds of the carbon atom are bonded to other carbon atoms.

X is not particularly limited, and examples of X include an alkylene group represented by the following general formula (11).
(Benz)-(CH ₂ ) _d -C(C _a H _2a+1 )(C _b H _2b+1 )-(CH ₂ ) _c -(R ₁₁ ) (11)
In formula (11), a, b, c, and d are integers satisfying 1≦a, 1≦b, 1≦c, 0≦d, and 3≦a+b+c+d≦19. ^R11 is ^R11 in formula (1). Benz is a benzene ring in formula (1) to which X is bonded.
In the above formula (11), it is preferable that a = 1 and b = 1, and it is particularly preferable that X is an alkylene group having a structural unit represented by the following formula (1X), from the viewpoint of obtaining excellent aldehyde isomer selectivity.
-C( _CH3 ) ₂ - _CH2- (1X)

From the viewpoint of achieving better aldehyde isomer selectivity, X is preferably an alkylene group having 4 to 20 carbon atoms including a quaternary carbon atom, more preferably an alkylene group having 4 to 10 carbon atoms including a quaternary carbon atom, still more preferably an alkylene group having 4 to 5 carbon atoms including a quaternary carbon atom, and particularly preferably an alkylene group represented by the following general formula (12), i.e., a 1,1-dimethylethylene group.
(Benz)-C( _CH3 ) ₂ - _CH2- ( _R11 ) (12)
In formula (12), R ¹¹ is R ¹¹ in formula (1) above. Benz is the benzene ring in formula (1) above to which X is bonded.

< ^R1 and ^R11 >
R ¹ and R ¹¹ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, and a cycloalkyl group having 3 to 20 carbon atoms.

Examples of the alkyl group having 1 to 20 carbon atoms include linear or branched alkyl groups such as methyl, ethyl, n-propyl, i-propyl, s-butyl, t-butyl, isopentyl, neopentyl, t-pentyl, t-hexyl, and 1,1,2-trimethylpropyl. Among these, those having 3 to 20 carbon atoms are preferred, those having 4 to 20 carbon atoms are more preferred, and those having 4 to 10 carbon atoms are particularly preferred. Furthermore, those in which the carbon atom bonded to X (in the case of R ¹¹ ) or the benzene ring (in the case of R ¹ ) in formula (1) is a tertiary carbon atom are preferred, and examples of such alkyl groups include t-butyl, t-pentyl, and t-hexyl groups.

Examples of cycloalkyl groups having 3 to 20 carbon atoms include cyclohexyl, cyclooctyl, and adamantyl groups. Among these, cycloalkyl groups having 6 to 14 carbon atoms are preferred, and cycloalkyl groups having 6 to 10 carbon atoms are more preferred.

R ¹ and R ¹¹ are preferably a tertiary alkyl group having 4 to 20 carbon atoms, more preferably a tertiary alkyl group having 4 to 7 carbon atoms, and particularly preferably a t-butyl group.

R ¹ and R ¹¹ may be the same or different.

When R ¹ and R ¹¹ are t-butyl groups, the compound represented by general formula (1) can be easily synthesized by reacting an inexpensive raw material such as isobutylene gas or t-butyl alcohol with a phenol such as phenol or cresol, which is the raw material for the compound. In addition, when R ¹ and R ¹¹ are t-butyl groups, the bulkiness of the t-butyl group provides a sufficient stabilizing effect against hydrolysis of the bisphosphite compound represented by general formula (2) described below.
For the above reasons, R ¹ and R ¹¹ are particularly preferably t-butyl groups.

<-X-R ¹¹ >
From the viewpoint of achieving better aldehyde isomer selectivity, a more specific embodiment of -X-R ¹¹ includes groups represented by formulae (a), (a'), and (b) to (g) in the following Table 1. In the following formulae (a), (a'), and (b) to (g), "*" indicates the bonding site of X in the above formula (1) to the benzene ring.

< ^R2 and ^R12 >
^R2 and ^R12 each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group and an alkoxy group having 1 to 20 carbon atoms, a cycloalkyl group and a cycloalkoxy group having 3 to 20 carbon atoms, a dialkylamino group having 2 to 20 carbon atoms, an aryl group and an aryloxy group having 6 to 20 carbon atoms, an alkylaryl group, an alkylaryloxy group, an arylalkyl group and an arylalkoxy group having 7 to 20 carbon atoms, a cyano group, a hydroxy group, and a halogen atom.

Examples of the alkyl group having 1 to 20 carbon atoms include linear or branched alkyl groups such as methyl, ethyl, n-propyl, i-propyl, n-butyl, s-butyl, t-butyl, n-pentyl, isopentyl, neopentyl, t-pentyl, and t-hexyl groups.
Examples of the cycloalkyl group having 3 to 20 carbon atoms include a cyclohexyl group, a cyclooctyl group, and an adamantyl group.

Examples of alkoxy groups having 1 to 20 carbon atoms include linear or branched alkoxy groups such as methoxy, ethoxy, isopropoxy, t-butoxy, etc. Among these, alkoxy groups having 1 to 12 carbon atoms are preferred.
Examples of the cycloalkoxy group having 3 to 20 carbon atoms include a cyclopentyloxy group.

Examples of the dialkylamino group having 2 to 20 carbon atoms include a dimethylamino group and a diethylamino group.
Examples of the aryl group having 6 to 20 carbon atoms include a phenyl group and a naphthyl group.
Examples of the aryloxy group having 6 to 20 carbon atoms include a phenoxy group and a naphthoxy group.
Examples of the alkylaryl group having 7 to 20 carbon atoms include a p-tolyl group and an o-tolyl group.

Examples of the alkylaryloxy group having 7 to 20 carbon atoms include a 2,3-xylenoxy group.
An example of the arylalkyl group having 7 to 20 carbon atoms is a benzyl group.
Examples of the arylalkoxy group having 7 to 20 carbon atoms include a 2-(2-naphthyl)ethoxy group.
Examples of the halogen atom include a fluorine atom, a chlorine atom, a bromine atom, and an iodine atom.

^R2 and ^R12 may be the same or different.

^R2 and ^R12 are preferably hydrogen atoms. Substituents at these positions have little effect on improving the reactivity in the hydroformylation reaction or on stabilizing the bisphosphite compound itself represented by the general formula (2) described below. Therefore, from the viewpoint of reducing the production cost of the compound, hydrogen atoms, which are the simplest substituents, are preferred.

< ^R3 and ^R13 >
^R3 and ^R13 each represent a member selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, and an alkylaryl group and an arylalkyl group having 7 to 20 carbon atoms.

Examples of alkyl groups having 1 to 20 carbon atoms include straight-chain or branched-chain alkyl groups such as methyl, ethyl, n-propyl, i-propyl, s-butyl, t-butyl, isopentyl, neopentyl, t-pentyl, and t-hexyl. Of these, those having 4 to 20 carbon atoms are preferred, and those having 4 to 10 carbon atoms are particularly preferred. Furthermore, those in which the carbon atom bonded to the aromatic ring is tertiary are preferred, and examples thereof include t-butyl, t-pentyl, and t-hexyl.

Examples of cycloalkyl groups having 3 to 20 carbon atoms include a cyclohexyl group, a cyclooctyl group, an adamantyl group, etc. Among these, a cycloalkyl group having 6 to 14 carbon atoms is preferred, and a cycloalkyl group having 6 to 10 carbon atoms is more preferred.
Examples of the aryl group having 6 to 20 carbon atoms include a phenyl group and a naphthyl group.
Examples of the alkylaryl group having 7 to 20 carbon atoms include a p-tolyl group and an o-tolyl group.
An example of the arylalkyl group having 7 to 20 carbon atoms is a benzyl group.

R ³ and R ¹³ are preferably a tertiary alkyl group having 4 to 20 carbon atoms, more preferably a tertiary alkyl group having 4 to 7 carbon atoms, and particularly preferably a t-butyl group.

^R3 and ^R13 may be the same or different.

The reason why ^R3 and ^R13 are particularly preferably t-butyl groups is that the dihydroxybiphenyl compound represented by the general formula (1) can be easily synthesized by reacting a phenol such as phenol or cresol, which is a raw material of the dihydroxybiphenyl compound, with an inexpensive raw material such as isobutylene gas or t-butyl alcohol.

< ^R4 and ^R14 >
^R4 and ^R14 each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms, an alkoxy group having 1 to 12 carbon atoms, a silyl group, a siloxy group, and a halogen atom.

Examples of the alkyl group having 1 to 12 carbon atoms include straight-chain or branched-chain alkyl groups such as methyl, ethyl, n-propyl, isopropyl, t-butyl, and decyl groups.
Examples of cycloalkyl groups having 3 to 12 carbon atoms include cyclopropyl and cyclohexyl groups.
Examples of alkoxy groups having 1 to 12 carbon atoms include straight-chain or branched-chain alkoxy groups such as methoxy, ethoxy, and t-butoxy groups.

An example of the silyl group is a trimethylsilyl group.
Examples of the siloxy group include a siloxy group and a trimethylsiloxy group.
Examples of the halogen atom include a fluorine atom, a chlorine atom, a bromine atom, and an iodine atom.

R ⁴ and R ¹⁴ may be the same or different.

Of these, R ⁴ and R ¹⁴ are each independently preferably a hydrogen atom, an alkyl group having 1 to 3 carbon atoms such as a methyl group or an ethyl group, an alkoxy group having 1 to 3 carbon atoms such as a methoxy group or an ethoxy group, or a halogen atom, more preferably an alkyl group having 1 to 3 carbon atoms, and particularly preferably both of them are a methyl group.

The reason why a small group such as an alkyl group having 1 to 3 carbon atoms, particularly a methyl group, is preferred as ^R4 and ^R14 is that it allows the coupling reaction described below to proceed smoothly while improving the stability of the bisphosphite compound represented by general formula (2) described below.

<Preferred embodiment>
The dihydroxybiphenyl compound represented by the general formula (1) is
Preferred is a dihydroxybiphenyl compound in which X is an alkylene group having 4 to 5 carbon atoms including a quaternary carbon atom, R ¹ and R ¹¹ are each independently a tertiary alkyl group having 4 to 20 carbon atoms, R ² and R ¹² are a hydrogen atom, R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 20 carbon atoms, and R ⁴ and R ¹⁴ are each independently selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, an alkoxy group having 1 to 3 carbon atoms, and a halogen atom.
The dihydroxybiphenyl compound represented by the general formula (1) is
More preferred is a dihydroxybiphenyl compound in which X is an alkylene group having a structural unit represented by formula (1X), R ¹ and R ¹¹ , R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 7 carbon atoms, R ² and R ¹² are hydrogen atoms, and R ⁴ and R ¹⁴ are each independently an alkyl group having 1 to 3 carbon atoms.
The dihydroxybiphenyl compound represented by the general formula (1) is
Particularly preferred are dihydroxybiphenyl compounds in which X is a 1,1-dimethylethylene group, R ¹ , R ¹¹ , R ³ and R ¹³ are t-butyl groups, R ² and R ¹² are hydrogen atoms, and R ⁴ and R ¹⁴ are methyl groups.

<Specific examples of dihydroxybiphenyl compounds>
Specific embodiments of the dihydroxybiphenyl compound of the present invention are not particularly limited. For example, the compounds exemplified as specific embodiments of the bisphosphite compound of the present invention shown below may be those in which the phosphate ester group is replaced with a hydroxyl group.

<Method of Producing Dihydroxybiphenyl Compound>
The method for producing the dihydroxybiphenyl compound of the present invention represented by the general formula (1) is not particularly limited. For example, as shown in the following reaction formula (X), the compound can be synthesized by applying the Suzuki-Miyaura cross-coupling reaction. That is, the compound can be synthesized by using a palladium catalyst having a phosphine ligand in the presence of a basic compound such as sodium carbonate from a boronic acid derivative of a corresponding phenol compound and a halide of the corresponding phenol compound.

In the above reaction formula (X), X, R ¹ to R ⁴ , and R ¹¹ to R ¹⁴ are respectively defined as X, R ¹ to R ^4, and R ¹¹ to R ¹⁴ in general formula (1), B represents a boron atom, and Br represents a bromine atom.

The dihydroxybiphenyl compound of the present invention represented by the general formula (1) can also be synthesized by an oxidative coupling reaction using a copper catalyst in the presence of methanol and air.

Below, an example of a method for producing the dihydroxybiphenyl compound of the present invention will be described using a production example of compound A represented by the following formula (A), which is one embodiment of the dihydroxybiphenyl compound of the present invention.

The method for producing a dihydroxybiphenyl compound of the present invention is not limited to these explanations. In addition to the examples below, a person skilled in the art can use well-known techniques to make appropriate modifications within the scope of the present invention to produce compound A and dihydroxybiphenyl compounds other than compound A.

First, a method for producing a compound (AR) having a phenol structure on the right side of compound A represented by formula (A) will be described.
First, a phenolic compound having no substitution at the ortho- and para-positions of the hydroxyl group is used as a starting material, and this is alkylated with isobutene to introduce tert-butyl groups into the ortho- and para-positions of the hydroxyl group. This alkylation reaction of phenols can generally be carried out using the Friedel-Crafts reaction in the presence of an acid catalyst. For example, as described in JP-A-55-81829, m-cresol and isobutene are reacted in the presence of 70% perchloric acid and 85% phosphoric acid catalyst to produce 4,6-di-tert-butyl-m-cresol (hereinafter referred to as "phenol-a"). This is the compound (A-R) (Reaction Formula-1).

Next, a method for producing the compound (AL) having a phenol structure on the left side of the compound A represented by formula (A) will be described.
First, the production of 2,4,4-trimethyl-1-pentene, which is the source of the 1,1,3,3-tetramethylbutyl group added to the ortho-position of the hydroxy group of compound (AL), will be described.
For the production of 2,4,4-trimethyl-1-pentene, a dimerization reaction of isobutene can be used. For example, as described in German Patent Application Publication No. 3542171, a mixture containing 2,4,4-trimethyl-1-pentene (hereinafter referred to as "diisobutene-a") and 2,4,4-trimethyl-2-pentene (hereinafter referred to as "diisobutene-b") represented by the following formula can be produced by reacting isobutene at high temperature on a zeolite catalyst to which bismuth or lead has been added (Reaction Formula 2).

The mixture obtained by the above-mentioned operation can be purified or separated by a known purification method or a known separation method to obtain diisobutene-a.
Next, m-cresol is used as a starting material and is alkylated with diisobutene-a to introduce diisobutene groups into only the ortho-position, only the para-position, or both the ortho-position and the para-position of the hydroxyl group. This alkylation reaction of phenols can generally be carried out using the Friedel-Crafts reaction in the presence of an acid catalyst. For example, a mixture containing 4-(1,1,3,3-tetramethylbutyl)-m-cresol (hereinafter referred to as "phenol-b"), 6-(1,1,3,3-tetramethylbutyl)-m-cresol (hereinafter referred to as "phenol-c"), and 4,6-di-(1,1,3,3-tetramethylbutyl)-m-cresol (hereinafter referred to as "phenol-d") can be produced by the Friedel-Crafts reaction of m-cresol and diisobutene-a (Reaction Scheme 3).

The mixture obtained by the above-mentioned procedure can be purified or separated using a known purification method or a known separation method to obtain phenol-c.

Then, phenol-c is used as the starting material and is alkylated with isobutene to introduce an isobutene group into the para-position of the hydroxyl group. This alkylation reaction of phenol-c can generally be carried out using the Friedel-Crafts reaction in the presence of an acid catalyst. For example, phenol-c and isobutene can be subjected to a Friedel-Crafts reaction to produce 4-tert-butyl-6-(1,1,3,3-tetramethylbutyl)-m-cresol (hereinafter referred to as "phenol-e"), which is the compound (A-L) (Reaction Scheme 4).

Compound A, which is one embodiment of the dihydroxybiphenyl compound of the present invention, can be produced by subjecting phenol-a (compound (A-R)) and phenol-e (compound (A-L)) to an oxidative coupling reaction. The oxidative coupling reaction can be carried out by optimizing the method described in The Journal of Organic Chemistry 1984, 49(23), 4456-4459 or The Journal of Organic Chemistry 1983, 48(25), 4948-4950 as appropriate based on well-known techniques by a person skilled in the art.

For example, the phenol-a and the phenol-e can be subjected to an oxidative coupling reaction in the presence of a copper chloride-tetramethylethylenediamine catalyst while blowing in air to produce a mixture containing 3,3',5,5'-tetra-tert-butyl-6,6'-dimethyl-1,1'-biphenyl-2,2'-diol (hereinafter referred to as "biphenol-a"), 3-(1,1,3,3-tetramethylbutyl)-3'-tert-butyl-5,5'-di-tert-butyl-6,6'-dimethyl-1,1'-biphenyl-2,2'-diol (corresponding to the compound A), and 3,3'-di-(1,1,3,3-tetramethylbutyl)-5,5'-di-tert-butyl-6,6'-dimethyl-1,1'-biphenyl-2,2'-diol (hereinafter referred to as "biphenol-b") (Reaction formula 5).

The mixture obtained by the above-mentioned operation can be purified or separated using a known purification method such as recrystallization or column purification, or a known separation method, to obtain Compound A, which is a dihydroxybiphenyl compound of the present invention.

Alternatively, another method for producing compound A may be as follows.
That is, when phenol-a is produced according to the above reaction formula-1, a small amount of phenol-e or 4-(1,1,3,3-tetramethylbutyl)-6-tert-butyl-m-cresol (hereinafter referred to as "phenol-f") shown below may be produced as an impurity. As described above, the produced phenol-e can be subjected to an oxidative coupling reaction with the above phenol-a to produce compound A. In addition, when phenol-f is contained, a small amount of 3,3'-di-tert-butyl-5-(1,1,3,3-tetramethylbutyl)-5'-tert-butyl-6,6'-dimethyl-1,1'-biphenyl-2,2'-diol (hereinafter referred to as "biphenol-g") shown below may be produced from phenol f.

[Bisphosphite compound]
The bisphosphite compound of the present invention is a novel bisphosphite compound represented by the following general formula (2).

In the above formula (2), X, R ¹ to R ⁴ , and R ¹¹ to R ¹⁴ are respectively defined as X, R ¹ to R ⁴ , and R ¹¹ to R ¹⁴ in the above formula (1). R ¹ and X-R ¹¹ are different from each other.
Z ¹ to Z ⁴ each independently represent an aryl group having 6 to 20 carbon atoms, and may have a substituent, and the substituents may be bonded to each other to form a ^ring .
and Z ² , and Z ³ and Z ⁴ may not be bonded to each other, or may be bonded to each other to form a ring structure.

<Z ¹ to Z ⁴ >
Z ¹ to Z ⁴ are each independently an aryl group having 6 to 20 carbon atoms, and the aryl group may have a substituent. The substituents may be bonded to each other to form a ring. Z ¹ and Z ² , and Z ³ and Z ⁴ may not be bonded to each other, or may be bonded to each other to form a ring structure containing -O-P-O-.

In particular, it is preferable that Z ¹ to Z ⁴ each independently have no substituent on the aromatic ring carbon atom adjacent to the carbon atom bonded to the oxygen atom, or even if the aromatic ring carbon atom has a substituent, the substituent has a carbon atom number of 0 to 2. When Z ¹ to Z ⁴ have a substituent, it is preferable that the substituent be located at the m-position or p-position relative to the carbon atom bonded to the oxygen atom.

When Z ¹ to Z ⁴ have a substituent on an aromatic ring carbon atom adjacent to the carbon atom bonded to an oxygen atom, the substituent is preferably selected from the group consisting of an alkyl group having 1 to 2 carbon atoms, such as a methyl group and an ethyl group, a trifluoromethyl group, a cyano group, a nitro group, and a halogen atom, such as a chlorine atom and a fluorine atom.

When Z ¹ to Z ⁴ have a substituent at a position other than the aromatic ring carbon atom adjacent to the carbon atom bonded to the oxygen atom, examples of the substituent include linear or branched alkyl groups having 1 to 12, preferably 1 to 8, carbon atoms, such as methyl, ethyl, n-propyl, i-propyl, n-butyl, s-butyl, t-butyl, n-pentyl, isopentyl, neopentyl, and t-pentyl groups, linear or branched alkoxy groups having 1 to 12, preferably 1 to 8, carbon atoms, such as methoxy and ethoxy groups, and aryl groups having 6 to 18, preferably 6 to 10, carbon atoms, such as phenyl and naphthyl groups. Other examples of the substituent include halogen atoms, cyano, nitro, trifluoromethyl, hydroxyl, amino, acyl, carbonyloxy, oxycarbonyl, amide, sulfonyl, sulfinyl, silyl, and thionyl groups. Each of Z ¹ to Z ⁴ may have 1 to 5 of these substituents.
Adjacent substituents may be bonded together to form a ring, such as a saturated hydrocarbon ring condensed with an aromatic ring of Z ¹ to Z ⁴ .

Preferred examples of Z ¹ to Z ⁴ include a phenyl group, a 1-naphthyl group, a 2-naphthyl group, a p-trifluoromethylphenyl group, a 2-ethylphenyl group, a 2-methylphenyl group, a 3-methylphenyl group, a 4-methylphenyl group, a 2,3-dimethylphenyl group, a 2,4-dimethylphenyl group, a 2,5-dimethylphenyl group, a 3,4-dimethylphenyl group, a 3,5-dimethylphenyl group, a 2-chlorophenyl group, a 3-chlorophenyl group, a 4-chlorophenyl group, a 2,3-dichlorophenyl group, a 2,4-dichlorophenyl group, a 2,5-dichlorophenyl group, a 3,4-dichlorophenyl group, Examples of the alkyl group include a chlorophenyl group, a 3,5-dichlorophenyl group, a 2-methoxyphenyl group, a 3-methoxyphenyl group, a 4-methoxyphenyl group, a 2,3-dimethoxyphenyl group, a 3,4-dimethoxyphenyl group, a 3,5-dimethoxyphenyl group, a 4-cyanophenyl group, a 4-nitrophenyl group, a 4-phenylphenyl group, a 5,6,7,8-tetrahydro-1-naphthyl group, a 5,6,7,8-tetrahydro-2-naphthyl group, a 2-methyl-1-naphthyl group, a 4-chloro-1-naphthyl group, a 2-nitro-1-naphthyl group, and a 7-methoxy-2-naphthyl group.
When Z ¹ and Z ² , and Z ³ and Z ⁴ are bonded to each other to form a ring structure containing --O--P--O--, suitable examples include a 1,1'-biphenyl-2,2'-diyl group, a 1,1'-binaphthyl-2,2'-diyl group, and the like.

Among these, Z ¹ to Z ⁴ are each preferably independently a 1-naphthyl group or a 2-naphthyl group from the viewpoints of improving the thermal stability of the ligand and improving the selectivity of linear aldehyde production when producing an aldehyde by hydroformylation reaction.

Z ¹ to Z ⁴ may be the same or different. As described later, from the viewpoint of ease of synthesis, it is preferable that Z ¹ and Z ² , Z ³ and Z ⁴ are the same, and it is more preferable that Z ¹ to Z ⁴ are all the same.

<Preferred embodiment>
The bisphosphite compound represented by the general formula (2) is preferably a bisphosphite compound in which X is an alkylene group having 4 to 5 carbon atoms including a quaternary carbon atom, R ¹ and R ¹¹ are each independently a tertiary alkyl group having 4 to 20 carbon atoms, R ¹ and X-R ¹¹ are different from each other, R ² and R ¹² are hydrogen atoms, R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 20 carbon atoms, and R ⁴ and R ¹⁴ are each independently selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, an alkoxy group having 1 to 3 carbon atoms, and a halogen atom.
Among the bisphosphite compounds represented by general formula (2), preferred are those in which Z ¹ to Z ⁴ each independently have no substituent on an aromatic ring carbon atom adjacent to a carbon atom bonded to an oxygen atom, or have a substituent having 1 to 2 carbon atoms on the aromatic ring carbon atom, and none of Z ¹ to Z ⁴ are bonded to each other.

Further, as the bisphosphite compound represented by the general formula (2), a bisphosphite compound in which X is an alkylene group having a structural unit represented by the above formula (1X), R ¹ , R ¹¹ , R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 7 carbon atoms, R ¹ and X-R ¹¹ are different from each other, R ² and R ¹² are a hydrogen atom, and R ⁴ and R ¹⁴ are each independently an alkyl group having 1 to 3 carbon atoms is more preferable.
As the bisphosphite compound represented by general formula (2), a bisphosphite compound in which Z ¹ to Z ⁴ are each independently a 1-naphthyl group or a 2-naphthyl group is more preferred, and a bisphosphite compound in which X is a 1,1-dimethylethylene group, R ¹ , R ¹¹ , R ³ and R ¹³ are t-butyl groups, R ² and R ¹² are hydrogen atoms, R ⁴ and R ¹⁴ are methyl groups, and Z ¹ to Z ⁴ are each independently a 1-naphthyl group or a 2-naphthyl group is particularly preferred.

<Specific examples of bisphosphite compounds>
Specific embodiments of the bisphosphite compound of the present invention include compounds represented by the following formulas (L-1-x) to (L-80-x), but are not limited to these compounds.
The symbol "x" in the formulae (L-1-x) to (L-80-x) is any one of the formulae (a), (a'), (b) to (g) shown in Table 1 above.

For example, the compound of the following formula (L-1-a) means that in the bisphosphite compound represented by the general formula (2), the substituent corresponding to -X-R ¹¹ is the substituent represented by formula (a) in Table 1.

In the compounds represented by the following formulas (L-1-x) to (L-80-x) (wherein x is a, a', b to g), x can be replaced with one selected from the group consisting of a, a', and b to g.
For example, in the compound of formula (L-1-a), "-a" can be replaced with "-b", and the substituent corresponding to -X-R ¹¹ of the bisphosphite compound represented by the general formula (2) can be replaced from the substituent represented by formula (a) in Table 1 above to the substituent represented by formula (b). Other substituents represented by formulas (a') and (c) to (g) can be replaced in the same manner.
For example, the structural formula of a compound in which "-a" in the compound of the following formula (L-1-a) is replaced with "-a'", "-b", "-c", "-d", "-e" and "-f" is shown below.

<Method for producing bisphosphite compound>
The method for producing the bisphosphite compound of the present invention represented by the general formula (2) is not particularly limited, and the compound can be synthesized by reacting an alkali metal salt or alkaline earth metal salt of a dihydroxybiphenyl compound represented by the following general formula (4) with a phosphorus compound represented by the following general formula (5A) and/or (5B) (bidentate phosphite synthesis method 1).
In general formula (4), X, R ¹ to R ⁴ , and R ¹¹ to R ¹⁴ are respectively defined as X, R ¹ to R ^4, and R ¹¹ to R ¹⁴ in general formula (2). M is an alkali metal or an alkaline earth metal. In general formulas (5A) and (5B), Z ¹ to Z ⁴ are respectively defined as Z ¹ to Z ⁴ in general formula (2).

Alternatively, the bisphosphite compound of the present invention represented by the general formula (2) can be synthesized by reacting an alkali metal salt or alkaline earth metal salt of a dihydroxybiphenyl compound represented by the general formula (4) with a bis(dialkylamino)chlorophosphine represented by the following general formula (6) to obtain a biphenyldioxy intermediate having two bis(dialkylamino)phosphino groups, which is then reacted with hydrogen chloride to obtain a biphenyldioxy intermediate having two dichlorophosphino groups, which is then reacted with a phenol in the presence of a base catalyst (bidentate phosphite synthesis method 2).
In the general formula (6), R ²⁰ represents a linear or branched alkyl group having 1 to 5 carbon atoms, such as a methyl group, an ethyl group, an n-propyl group, or an i-propyl group.

The following provides a detailed explanation of bidentate phosphite synthesis method 1. Details of bidentate phosphite synthesis method 2 are described in JP 2000-53688 A.

The alkali metal salt or alkaline earth metal salt of the dihydroxybiphenyl compound represented by the above general formula (4) can be synthesized by reacting the dihydroxybiphenyl compound of the present invention represented by the above general formula (1) with an alkali metal compound such as n-BuLi (normal butyl lithium), Na, NaH or KH, or an alkaline earth metal compound such as methylmagnesium bromide or ethylmagnesium bromide, in a solvent, preferably in an inert gas atmosphere such as nitrogen.

The amount of the alkali metal compound or alkaline earth metal compound used is usually 2 moles per mole of the dihydroxybiphenyl compound represented by general formula (1), but more may be used if desired.

As the solvent, ethers such as tetrahydrofuran and diethyl ether, hydrocarbons such as hexane and toluene, nitrogen-containing compounds such as pyridine, triethylamine and N,N,N',N'-tetramethylethylenediamine, and mixtures thereof are preferably used.

The reaction temperature can be appropriately selected within the range of −70° C. to the boiling point of the solvent. A method can also be adopted in which the reaction is started at a low temperature, for example, between −30° C. and 10° C., and then gradually increased to the boiling point of the solvent.
From the viewpoint of reaction operation, it is preferable to carry out the reaction using n-BuLi or NaH and tetrahydrofuran as a solvent.

The reaction time can usually be selected within the range of 1 minute to 48 hours, and is preferably about 10 minutes to 4 hours.
After synthesizing the alkali metal salt or alkaline earth metal salt of the dihydroxybiphenyl compound represented by the general formula (4), the reaction solution may be used in the next step as it is without any particular purification. After synthesizing the alkali metal salt or alkaline earth metal salt of the dihydroxybiphenyl compound represented by the general formula (4), the compound may be used in the next step after previously carrying out a treatment such as washing with a poor solvent or isolation by a recrystallization operation.

The phosphorus compound represented by the general formula (5A) or (5B) can be synthesized by reacting phosphorus trichloride (PCl ₃ ) with a phenol represented by Z ¹ -OH, Z ² -OH, Z ³ -OH or Z ⁴ -OH (wherein Z ¹ to Z ⁴ have the same meaning as Z ¹ to Z ⁴ in the general formula (2)) in the presence or absence of a base, preferably in an inert gas atmosphere such as nitrogen, in a solvent or without a solvent.

A phosphorus compound in which ^Z1 and ^Z2 or ^Z3 and ^Z4 are the same is preferred because it can be easily synthesized. Therefore, it is preferred that ^Z1 and ^Z2 , and ^Z3 and ^Z4 are both the same, and it is particularly preferred that ^Z1 to ^Z4 are all the same.

When a base is used, examples of the base include nitrogen-containing bases such as pyridine, triethylamine, and diethylamine, and inorganic bases such as sodium carbonate and potassium carbonate. Among them, nitrogen-containing bases are preferably used because of the ease of reaction operation. The amount of base used is usually 2 moles per mole of PCl _3. If the amount of base is too large or too small, it is not preferable because it increases the amount of unnecessary phosphites such as P(OZ ¹ ) ₂ (OZ ² ), P(OZ ¹ ) (OZ ² ) ₂ , P(OZ ¹ ) _{3 , and P(OZ 2 ) 3} ^and dichloro compounds such as Cl ₂ P ₍ OZ ¹ ).

The reaction temperature can be selected arbitrarily. For example, when a nitrogen-containing base is used as the base, the reaction is preferably carried out at a temperature of 0 to 5°C.
The reaction time can be selected within the range of 1 minute to 48 hours. For example, a reaction time of about 5 minutes to 10 hours is preferred.

When the reaction is carried out in the presence of a base, the by-product of the reaction, a salt of hydrogen chloride and a base, is usually present as a solid in the reaction solution. The by-product of the salt of hydrogen chloride and a base can be removed from the reaction system by filtration or other methods, preferably under an inert gas atmosphere such as nitrogen. When the reaction is carried out in the absence of a base, the by-product of hydrogen chloride can be removed from the reaction system by bubbling an inert gas such as nitrogen gas or argon gas into the reaction system.

The phosphorus compound represented by the general formula (5A) or (5B) may be obtained as a mixture with the unnecessary phosphites and dichloro compounds. These may be used in the next step without being separated. Methods for separating the phosphorus compound represented by the general formula (5A) or (5B) from these by-products include recrystallization using an aliphatic hydrocarbon solvent such as hexane or heptane, and distillation.

The bisphosphite compound of the present invention represented by the general formula (2) can be synthesized by contacting the compound represented by the general formula (4) with the compound represented by the general formula (5A) and/or (5B) in a solvent or without a solvent at a temperature of 20°C or less for 1 minute or more.

The above contact is preferably carried out under an inert gas atmosphere such as nitrogen, and the target bisphosphite compound can be synthesized by mixing the compound represented by the general formula (4) with the compound represented by the general formula (5A) and/or (5B) at a temperature of preferably 0°C or lower, more preferably -30°C or lower, and most preferably -50°C or lower, maintaining that temperature for 1 minute or more, preferably 3 to 60 minutes, and then gradually increasing the temperature.

The rate of temperature increase can be selected appropriately between 0.1 and 20°C/min. A rate of temperature increase between 0.5 and 10°C/min is preferable.

When a solvent is used, the solvent may be ethers such as tetrahydrofuran, diethyl ether, and dioxane, hydrocarbons such as hexane and toluene, nitrogen-containing compounds such as pyridine, triethylamine, and N,N,N',N'-tetramethylethylenediamine, or mixtures thereof.

The amount of solvent used should be the minimum necessary to dissolve the product, but more than this amount may be used.

　Methods for purifying the bisphosphite compound of the present invention represented by the general formula (2) include a column chromatography method, a suspension washing method, and a recrystallization method.

Examples of the column development method include a method using silica gel, alumina, or the like as a packing material.
Examples of the developing solution for the column include ethers such as tetrahydrofuran and dioxane, aliphatic hydrocarbons such as hexane and heptane, aromatic hydrocarbons such as toluene and xylene, esters such as ethyl acetate and methyl acetate, and halogenated hydrocarbons such as chloroform and dichloromethane. These developing solutions are used alone or in combination with two or more solvents depending on the purification of the target product.

An example of the suspension washing method is a method in which, after completion of the synthesis reaction of the bisphosphite compound, by-produced metal chlorides (MCl or _MCl2 : M is an alkali metal or alkaline earth metal) are removed from the reaction solution by filtration or with a polar solvent such as water, the solution is evaporated to dryness, and the residue is stirred in a solvent such as acetonitrile, aliphatic hydrocarbons such as hexane and heptane, ketones such as acetone and diethyl ketone, or alcohols such as methanol and ethanol. In this way, the target product can be purified by dissolving unnecessary substances in a solvent without dissolving the target product in the solvent.

　Examples of the recrystallization method include a method in which, after the completion of the synthesis reaction of the bisphosphite compound, the by-produced metal chloride is removed from the reaction solution by filtration or with a polar solvent such as water, the solution is evaporated to dryness, and the residue is dissolved in the minimum amount of solvent that can dissolve it, and then cooled, or a method in which the residue is dissolved in the minimum amount of solvent that can dissolve it, a solvent in which the target bisphosphite compound is insoluble or poorly soluble is added, and cooling is performed as desired to precipitate a solid, which is then separated by a method such as filtration, and further washed with an insoluble solvent.

Examples of solvents in which the bisphosphite compound is soluble include aromatic hydrocarbons such as benzene, toluene, and xylene, and ethers such as tetrahydrofuran and dioxane.
Examples of solvents in which the bisphosphite compound is insoluble or poorly soluble include, in addition to acetonitrile, aliphatic hydrocarbons such as hexane and heptane, ketones such as acetone and diethyl ketone, and alcohols such as methanol and ethanol.

In the present invention, by carrying out a hydroformylation reaction using the novel bisphosphite compound described above, it is possible to achieve excellent selectivity for the target product.

Compositions containing the bisphosphite compound of the present invention, such as mixtures of the novel bisphosphite compound of the present invention with other bisphosphite compounds, are included in the embodiments of the present invention. In this case, the mixing ratio is not particularly limited. Examples of such mixtures include mixtures of the bisphosphite compound of the present invention with the bisphosphite compounds shown below that are by-produced during the production of the dihydroxybiphenyl compound (A) of the present invention and are derived from the crosslinked structure of the above-mentioned (biphenol-a) or (biphenol-g).

[catalyst]
The catalyst of the present invention contains a complex of the bisphosphite compound of the present invention and a metal of Groups 8 to 10. The catalyst of the present invention is useful as a catalyst for producing an aldehyde by reacting an olefin compound with carbon monoxide and hydrogen.
Examples of the olefin include those described in the section on the production method of aldehyde described below.

The complex containing the bisphosphite compound of the present invention and a Group 8-10 metal can be easily prepared from a Group 8-10 metal compound and the bisphosphite compound of the present invention by a known complex formation method.

Examples of the Group 8 to 10 metal compound used in the production of the complex include hydrides, halides, organic acid salts, inorganic acid salts, oxides, carbonyl compounds, amine compounds, olefin coordination compounds, phosphine coordination compounds, and phosphite coordination compounds of Group 8 to 10 metals. For example, ruthenium compounds such as ruthenium trichloride, dichloro(p-cymene)ruthenium dimer, and dichlorotris(triphenylphosphine)ruthenium; palladium compounds such as palladium acetate and palladium chloride; osmium compounds such as osmium trichloride; iridium compounds such as iridium trichloride and iridium carbonyl; platinum compounds such as platinic acid, sodium hexachloroplatinate, and potassium platinic acid; cobalt compounds such as dicobalt octacarbonyl and cobalt stearate; rhodium trichloride, rhodium nitrate, rhodium acetate, Rh(acac)(CO) ₂ , [Rh(OAc)(cod)] ₂ , _Rh4 (CO) ₁₂ , _Rh6 (CO) ₁₆ , HRh(CO( _PPh3 ) ₃ , [Rh(OAc)(CO) ₂ ] ₂ rhodium compounds such as [Rh(μ-S(t-Bu))(CO) ₂ ] ₂ and [RhCl(cod)] ₂ (in this specification, acac represents an acetylacetonato group, OAc represents an acetyl group, cod represents 1,5-cyclooctadiene, Ph represents a phenyl group, and t-Bu represents a t-butyl group). However, the present invention is not limited to these. These may be used alone or in combination of two or more.
Of these, cobalt, rhodium or ruthenium compounds are preferred, with rhodium compounds being particularly preferred.

In the catalyst of the present invention, the molar ratio of the bisphosphite compound to the Group 8 to 10 metal is preferably 0.00004 to 500, more preferably 0.0002 to 100, even more preferably 0.001 to 50, and particularly preferably 0.01 to 30. If the molar ratio of the bisphosphite compound to the Group 8 to 10 metal is within the above range, an excellent balance between catalyst cost and reaction efficiency improvement effect is achieved.

[Catalyst composition]
The catalyst composition of the present invention is one embodiment of a catalyst composition utilizing the bisphosphite compound of the present invention, and contains a bisphosphite compound represented by the following general formula (3) and the bisphosphite compound of the present invention represented by the general formula (2).
The catalyst composition of the present invention is useful as a catalyst composition for the production of aldehydes by reacting olefinic compounds with carbon monoxide and hydrogen.

(In formula (3),
R ¹ , R ² and R ¹² , R ³ and R ¹³ , R ⁴ and R ¹⁴ , and Z ¹ to Z ⁴ are respectively defined as R ¹ , R ² and R ¹² , R ³ and R ¹³ , R ⁴ and R ¹⁴ , and Z ¹ to Z ⁴ in the general formula (2).

Examples of the olefin include those described in the section on the method for producing aldehydes below.

More specifically, examples of the catalyst composition of the present invention include a catalyst composition containing a complex of a bisphosphite compound of the present invention represented by the general formula (3) and a metal of Groups 8 to 10, and a complex of a bisphosphite compound of the present invention represented by the formula (2) and a metal of Groups 8 to 10.

The catalyst composition of the present invention can be easily prepared from a Group 8 to 10 metal compound, a bisphosphite compound represented by the general formula (3) above, and a bisphosphite compound of the present invention represented by the formula (2) above, by a known complex formation method.

The Group 8 to 10 metal compound used in the production of the catalyst composition of the present invention is synonymous with the Group 8 to 10 metal compound in the catalyst of the present invention.

In the catalyst composition of the present invention, the molar ratio of the bisphosphite compound of the present invention represented by the above formula (2) to the Group 8 to 10 metal is synonymous with the molar ratio of the bisphosphite compound of the present invention to the Group 8 to 10 metal compound in the catalyst of the present invention.
In the catalyst composition of the present invention, the molar ratio of the bisphosphite compound represented by the general formula (3) to the Group 8 to 10 metal is synonymous with the molar ratio of the bisphosphite compound represented by the general formula (3) to the Group 8 to 10 metal compound in the catalyst of the present invention.

The lower limit of the content of the bisphosphite compound represented by the general formula (3) in the catalyst composition of the present invention is not particularly limited, but is preferably 100% by mass of the catalyst composition.
It can be 80.00% by mass or more,
More preferably 90.00% by mass or more,
More preferably, the content is 95.00% by mass or more.
It is particularly preferably 98.00% by mass or more.
More preferably, the content is 99.00% by mass or more.
It is even more preferable that the content is 99.40% by mass or more.
On the other hand, the lower limit of the content of the bisphosphite compound represented by the general formula (3) in the catalyst composition of the present invention is not particularly limited, but is preferably 100% by mass of the catalyst composition.
It can be 99.99% by mass or less,
More preferably 99.98% by mass or less,
More preferably, it is 99.97% by mass or less.
Particularly preferably 99.95% by mass or less,
It is particularly preferably 99.90% by mass or less,
It is most preferably 99.85% by mass or less.
The above upper and lower limits can be combined in any combination. For example, the content of the bisphosphite compound represented by the general formula (3) in the catalyst composition of the present invention is not particularly limited, but may be, for example, 100% by mass of the catalyst composition.
The content can be 80.00% by mass or more and 99.99% by mass or less,
More preferably, the content is 90.00% by mass or more and 99.98% by mass or less.
More preferably, the content is 95.00% by mass or more and 99.97% by mass or less.
Particularly preferably 98.00% by mass or more and 99.95% by mass or less,
Particularly preferably from 99.00% by mass to 99.90% by mass,
The most preferred range is 99.40% by mass or more and 99.85% by mass or less.

The lower limit of the content of the bisphosphite compound of the present invention represented by the formula (2) in the catalyst composition of the present invention is not particularly limited, but is preferably 100% by mass of the catalyst composition.
It can be 0.01% by mass or more,
More preferably, it is 0.02% by mass or more.
More preferably, the content is 0.03% by mass or more.
It is particularly preferably 0.05 mass % or more.
Particularly preferably 0.10% by mass or more,
It is most preferably 0.15 mass % or more.
On the other hand, the lower limit of the content of the bisphosphite compound of the present invention represented by the formula (2) in the catalyst composition of the present invention is not particularly limited, but is preferably 100% by mass of the catalyst composition.
It can be 20.00 mass% or less,
More preferably 10.00% by mass or less,
More preferably, it is 5.00% by mass or less.
Particularly preferably 2.00% by mass or less,
It is particularly preferably 1.00% by mass or less,
A content of 0.60 mass % or less is most preferable.
The above upper and lower limits can be combined in any combination. For example, the content of the bisphosphite compound of the present invention represented by the formula (2) in the catalyst composition of the present invention is not particularly limited, but may be, for example, 100% by mass of the total catalyst composition.
The content can be 0.01% by mass or more and 20.00% by mass or less,
More preferably, the content is 0.02% by mass or more and 10.00% by mass or less.
More preferably, the content is 0.03% by mass or more and 5.00% by mass or less.
Particularly preferably, the content is 0.05% by mass or more and 2.00% by mass or less.
Particularly preferably, the content is 0.10% by mass or more and 1.00% by mass or less.
The most preferred range is 0.15 mass % or more and 0.60 mass % or less.

The catalyst and catalyst composition of the present invention are used, for example, in the production of aldehydes from olefins, as shown below.

[Method for producing aldehyde]
The method for producing an aldehyde of the present invention is characterized by reacting an olefin compound with carbon monoxide and hydrogen in the presence of a Group 8 to 10 metal compound and the bisphosphite compound of the present invention.
Alternatively, the method for producing an aldehyde of the present invention is characterized by reacting an olefin compound with carbon monoxide and hydrogen in the presence of the above-mentioned catalyst of the present invention.

There are no particular limitations on the olefin compound, so long as it is an organic compound that has at least one olefinic double bond in the molecule. Specific examples include ethylene, propylene, butene, butadiene, pentene, hexene, hexadiene, octene, octadiene, decene, hexadecene, octadecene, icosene, docosene, styrene, α-methylstyrene, cyclohexene, and mixtures of lower olefins such as mixtures of propylene and butene, mixtures of 1-butene, 2-butene, and isobutylene, and mixtures of 1-butene, 2-butene, isobutylene, and butadiene; mixtures of olefin oligomer isomers such as dimers, trimers, and tetramers of lower olefins such as propylene, n-butene, and isobutylene; acrylonitrile, allyl alcohol, 1-hydroxy-2,7-octadiene, 3-hydroxy-1,7-octadiene, oleyl alcohol, 1-methoxy-2,7-octadiene, methyl acrylate, methyl methacrylate, and methyl oleate, and other polar group-substituted olefins.

The above olefin compounds can be used to carry out a hydroformylation reaction to produce the corresponding aldehydes. In general, the production ratio (L/B) of the linear aldehyde (L form) and branched aldehyde (B form) obtained is preferably 1 or more, more preferably 5 or more, and even more preferably 10 or more.

In the method for producing an aldehyde of the present invention, the Group 8 to 10 metal compound used as a catalyst or a precursor thereof may be a hydride, a halide, an organic acid salt, an inorganic acid salt, an oxide, a carbonyl compound, an amine compound, an olefin coordination compound, a phosphine coordination compound, or a phosphite coordination compound of a Group 8 to 10 metal. For example, ruthenium compounds such as ruthenium trichloride, dichloro(p-cymene)ruthenium dimer, and dichlorotris(triphenylphosphine)ruthenium; palladium compounds such as palladium acetate and palladium chloride; osmium compounds such as osmium trichloride; iridium compounds such as iridium trichloride and iridium carbonyl; platinum compounds such as platinic acid, sodium hexachloroplatinate, and potassium platinic acid; cobalt compounds such as dicobalt octacarbonyl and cobalt stearate; rhodium trichloride, rhodium nitrate, rhodium acetate, Rh(acac)(CO) ₂ , [Rh(OAc)(cod)] ₂ , _Rh4 (CO) ₁₂ , _Rh6 (CO) ₁₆ , HRh(CO( _PPh3 ) ₃ , [Rh(OAc)(CO) ₂ ] ₂ rhodium compounds such as [Rh(μ-S(t-Bu))(CO) ₂ ] ₂ and [RhCl(cod)] ₂ (in this specification, acac represents an acetylacetonato group, OAc represents an acetyl group, cod represents 1,5-cyclooctadiene, Ph represents a phenyl group, and t-Bu represents a t-butyl group), but are not necessarily limited to these. Among these, cobalt, rhodium, or ruthenium compounds are preferred, and rhodium compounds are particularly preferred.

The method for producing an aldehyde of the present invention can be carried out in the presence of a catalyst containing a complex formed in advance between the bisphosphite compound of the present invention and the above-mentioned Group 8 to 10 metal. The Group 8 to 10 metal complex containing the bisphosphite compound of the present invention can be easily prepared from a Group 8 to 10 metal compound and the bisphosphite compound by a known complex formation method.
In some cases, the Group 8 to 10 metal compound and the bisphosphite compound may be fed to the hydroformylation reaction zone to form a complex within the hydroformylation reaction system.

When a complex between a bisphosphite compound and a Group 8-10 metal is formed in advance and the aldehyde production method of the present invention is carried out in the presence of a catalyst containing the complex, for the same reasons as for the molar ratio of the bisphosphite compound to the Group 8-10 metal in the catalyst of the present invention described above, the molar ratio of the bisphosphite compound to the Group 8-10 metal is preferably 0.00004 to 500, more preferably 0.0002 to 100, even more preferably 0.001 to 50, and particularly preferably 0.01 to 30.

In the aldehyde production method of the present invention, the amount of the complex used is not particularly limited, and there are limitations based on considerations of catalytic activity and economic efficiency, but the complex is usually supplied to the reaction zone so that the concentration of Group 8 to 10 metal in the reaction solution in the hydroformylation reaction zone is preferably 0.05 to 5000 mg/L, more preferably 0.5 to 1000 mg/L, and even more preferably 5 to 500 mg/L, calculated as metal atoms.

If the concentration of the catalyst, Group 8 to 10 metal, is too low, there is a concern that sufficient reactivity will not be achieved. If the concentration of the Group 8 to 10 metal is too high, there is a concern that the cost of the catalyst will be too high. In addition, if too little bisphosphite compound is used, there is a concern that sufficient reactivity will not be achieved. If too much bisphosphite compound is used, there is a concern that the cost of the bisphosphite compound will be too high.

Similarly, when a Group 8 to 10 metal compound and a bisphosphite compound are supplied to a hydroformylation reaction zone to form a complex there, the amount of Group 8 to 10 metal compound used is not particularly limited and is limited by considerations of catalyst activity, economics, etc., but in the present invention, the concentration of the Group 8 to 10 metal compound in the reaction liquid in the hydroformylation reaction zone is preferably 0.05 to 5000 mg/L, more preferably 0.5 to 1000 mg/L, and even more preferably 5 to 500 mg/L, calculated as metal atoms.

If the concentration of the catalyst, a Group 8 to 10 metal, is too low, there is a concern that sufficient reactivity will not be achieved. If the concentration of the Group 8 to 10 metal is too high, there is a concern that the cost of the catalyst will be too high.

The amount of the bisphosphite compound used is not particularly limited, and is appropriately set so as to obtain the desired results in terms of catalyst activity and selectivity. Usually, it is 0.00004 to 500 moles, preferably 0.0002 to 100 moles, more preferably 0.001 to 50 moles, and most preferably 0.01 to 30 moles per mole of Group 8 to 10 metal. If the amount of the bisphosphite compound used is too small, there is a concern that sufficient reactivity will not be obtained. If the amount of the bisphosphite compound used is too large, there is a concern that the cost of the bisphosphite compound will be too high.

In the process for producing an aldehyde of the present invention, the use of a reaction solvent is not essential, but a solvent inert to the hydroformylation reaction can be present, if necessary.
Specific examples of preferred solvents include aromatic hydrocarbons such as toluene, xylene, and todecylbenzene; ketones such as acetone, diethyl ketone, and methyl ethyl ketone; ethers such as tetrahydrofuran and dioxane; esters such as ethyl acetate and di-n-octyl phthalate; high-boiling point components by-produced during the hydroformylation reaction, such as aldehyde condensates; and olefin compounds which are reaction raw materials.

The reaction conditions for carrying out the aldehyde production method of the present invention are similar to those commonly used in the past, and the reaction temperature is usually selected from the range of 15 to 200°C, preferably 50 to 150°C. The carbon monoxide partial pressure and hydrogen partial pressure are usually selected from the range of 0.0001 to 20 MPaG, preferably 0.01 to 10 MPaG, and particularly preferably 0.1 to 5 MPaG.

The molar ratio of carbon monoxide to hydrogen (H ₂ /CO) is usually selected from the range of 10/1 to 1/10, preferably 3/1 to 1/3.
The reaction can be carried out in a stirred reactor or a bubble column reactor either continuously or batchwise.

The reaction time is not particularly limited as long as it is a time that satisfactorily achieves the production of the target aldehyde, and can be appropriately selected based on the catalyst concentration, reaction conditions, reactor size, and other conditions. Typical reaction times are 1 minute to 100 hours, preferably 5 minutes to 20 hours, and more preferably 20 minutes to 10 hours.

In the method for producing an aldehyde of the present invention, the produced aldehyde is separated by a method such as distillation, and then the recovered liquid containing the Group 8 to 10 metal and the bisphosphite compound can be used to carry out the hydroformylation reaction of the olefin compound again.

Furthermore, when continuously converting olefin compounds to aldehydes, the remaining reaction liquid after separating some or all of the aldehyde produced can be continuously circulated to the hydroformylation reaction tank as a catalyst liquid.

[Method of producing alcohol]
The alcohol production method of the present invention is a method for producing an alcohol, which comprises producing an aldehyde by the aldehyde production method of the present invention and producing a corresponding alcohol from the aldehyde.

The method for producing the alcohol corresponding to the aldehyde is not particularly limited and can be carried out according to a conventional method. For example, according to the method described in JP 2001-10999 A, the aldehyde obtained by the aldehyde production method of the present invention can be directly subjected to a known hydrogenation reaction, or the obtained aldehyde can be dimerized and then subjected to a known hydrogenation reaction to produce an alcohol.

The hydrogenation catalyst used in the hydrogenation reaction may be a known solid catalyst in which a metal such as Ru, Ni, Cr, Cu, etc. is supported on a carrier. As the hydrogenation catalyst, a Ru-based catalyst is preferred.
The conditions for the hydrogenation reaction are usually a temperature of 60 to 200° C. and a hydrogen pressure of about 0.1 to 20 MPaG.

The present invention will be described in more detail below with reference to the following Experimental Examples, which are alternatives to the working examples, but are not intended to limit the scope of the present invention.
The following experimental examples are merely illustrative and are not intended to limit any of the embodiments described herein. The following experimental examples are not intended to limit the invention in any way.
The values of various manufacturing conditions and evaluation results in the following experimental examples are meant as preferred upper or lower limit values in the embodiments of the present invention, and a preferred range may be a range defined by a combination of the above-mentioned upper or lower limit values and the values of the following experimental examples or values of the experimental examples.

[raw materials]
The abbreviations of the compounds used in the experimental examples are as follows.
DBMC: 4,6-di-t-butyl-m-cresol [Rh(OAc)(cod)] ₂ : (1,5-cyclooctadiene)acetate rhodium dimer (product name: Rh ₂ (cod) ₂ (OAc) ₂ , manufactured by N.E. Chemcat Corporation)
Phosphite ligand A: a symmetric bisphosphite compound having only a t-Bu group at the o-position of the phosphite substituent, represented by the following structural formula, produced by the method described in Example 11 of Japanese Patent No. 3812046.

[Evaluation method]
In the following experimental examples, various physical properties were measured by the following methods.

<Measurement of molecular weight of compound A>
The molecular weight of Compound A was measured by high performance liquid chromatography mass spectrometry (LC/MS) under the following measurement conditions.
(LC measurement conditions)
High-performance liquid chromatogram device: Agilent 1260 (device name, manufactured by Agilent Technologies, Inc.)
Analytical column: CAPCELLPAK C18 MGIII (product name, manufactured by Osaka Soda Co., Ltd., size: inner diameter 4.6 mm × length 75 mm, film thickness 3 μm)
Eluent: acetonitrile Flow rate: 1.0 mL/min
Detector: UV detector (wavelength 210 nm)
Injection volume: 2 μL
(MS measurement conditions)
Mass spectrometer: Agilent LC/MS 6130 (instrument name, manufactured by Agilent Technologies, Inc.)
Ion source: Electrospray ionization (ESI) method (Positive/Negative; using AJS probe)
As an ionization assistant, a 20 mM aqueous solution of ammonium formate was added to the post-column at 0.1 mL/min.

<Structural analysis of compound A>
The structure of Compound A was analyzed using a nuclear magnetic resonance spectrometer (apparatus name: JNM-ECS400 type apparatus, manufactured by JEOL Ltd., resonance frequency ( ¹ H): 400 MHz, probe: H5XAT/FG2 (inverse)) according to the following procedure.
The isolated compound A was dissolved in deuterated chloroform (CDCl ₃ ) containing a small amount of tetramethylsilane (TMS) to prepare a sample for NMR measurement.
( ^1H -NMR measurement)
The obtained NMR measurement sample was subjected to ¹ H-NMR measurement using a nuclear magnetic resonance spectrometer under conditions of a measurement temperature of 25° C. and an accumulation number of 128.
( ^13C -NMR measurement)
The obtained NMR measurement sample was subjected to 13C-NMR (accumulation number: 3000 times), DEPT (flip angle: 135°, accumulation number: 3000 times), HMQC (accumulation number: 16 times), and HMBC (accumulation number: 8 times) measurements using a nuclear magnetic resonance spectrometer at a measurement temperature of ²⁵ °C under the following measurement conditions.

<Accurate Mass Measurement of Compound B>
The exact mass of the isolated compound B was measured using a liquid chromatograph/time-of-flight mass spectrometer (LC/ToFMS) under the following measurement conditions.
(Measurement conditions)
High-performance liquid chromatogram measuring device: Waters Acquity H-Class (device name, manufactured by Nihon Waters K.K.)
Analytical column: ACQUITY UPLC BEH C8 (product name, column size: inner diameter: 2.1 mm × column length: 100 mmL, film thickness: 1.7 μm, manufactured by Nihon Waters K.K.)
Eluent: acetonitrile Eluent flow rate: 0.4 mL/min
Mass spectrometer: Quadrupole-time-of-flight mass spectrometer Waters Xevo G2-XS Qtof (instrument name, manufactured by Nihon Waters K.K.)
Ionization method: Electrospray ionization (ESI) method (Positive Mode)
Mass calibrant: leucine enkephalin (RE)

<Structural analysis of compound B>
The structure of Compound B was analyzed using a nuclear magnetic resonance spectrometer (apparatus name: Bruker AVANCE NEO 600 type apparatus, manufactured by Bruker Corporation, resonance frequency ( ¹ H): 600 MHz, probe: 5 mm BBO Cryo) according to the following procedure.
The isolated compound B was dissolved in deuterated chloroform (CDCl ₃ ) containing a small amount of tetramethylsilane (TMS) to prepare a sample for NMR measurement.
( ^1H -NMR measurement)
The obtained NMR measurement sample was subjected to ¹ H-NMR measurement using a nuclear magnetic resonance spectrometer at a measurement temperature of 25° C. and an accumulation number of 16.
( ^13C -NMR measurement)
The obtained NMR measurement sample was measured using a nuclear magnetic resonance spectrometer at a measurement temperature of 25° C. under the following measurement conditions: ¹³ C-NMR (accumulation number: 256 times), DEPT (flip angle: 135°, accumulation number: 128 times), HSQC (accumulation number: 16 times), HMBC (accumulation number: 2 times), and ¹ H- ¹ H COSY (accumulation number: 2 times).

<IR Measurement of Compound B>
The isolated compound B was subjected to infrared spectroscopy (IR) measurement by an attenuated total reflection (ATR) method under the following measurement conditions using an infrared microscope (device name: Nicolet iN10MX, manufactured by Thermo Fisher Scientific Co., Ltd.) equipped with an FT-IR module (product name: iZ10, manufactured by Thermo Fisher Scientific Co., Ltd.).
(Measurement conditions)
ATR: Gladi ATR vision Diamond Crystal (PIKE)
Resolution: 4cm ^-1
Number of times: 64

[Example 1: Production of dihydroxybiphenyl compound of the present invention (compound A)]
In the production of a dihydroxybiphenyl compound (compound A), a composition containing DBMC (DBMC composition) was used as a starting material. The composition of the DBMC composition was analyzed using a gas chromatogram (GC) measurement device and a gas chromatography total area method under the following GC measurement conditions. As a result, the DBMC composition contained 97.5 GC area % of DBMC and 0.8 GC area % of a compound represented by the following formula (E) (the above-mentioned "phenol-e").
The composition ratio of each component in the gas chromatography total area method was calculated as the area content ratio (unit: GC area%) of each peak component when the total area of the GC peaks of all products on the gas chromatogram was taken as 100%.

<GC measurement conditions>
GC device: GC-2025 (high-performance general-purpose gas chromatograph, manufactured by Shimadzu Corporation)
Detector: Flame ionization detector (FID)
Carrier gas: nitrogen gas (column flow rate 4.07 mL/min)
Column: Capillary column BPX5 (manufactured by SGE Analytical Science, size: length 60 m x inner diameter 0.32 mm, film thickness 0.25 μm)
Column temperature: 50°C (holding time 5 minutes) → heating at 10°C/min → 300°C (holding time 10 minutes)
Inlet temperature: 300℃
Detector temperature: 300°C
Sample volume: 0.5 μL (split ratio: 1/20)

About 200 g of the DBMC composition was placed in a glass distillation apparatus, and 160 g of DBMC, the main component of the DBMC composition, was distilled off using an oil bath set at about 140°C under a reduced pressure of 3 mmHg. The residue in the distillation apparatus was removed and transferred to a glass reactor equipped with an air-blowing pipe, and 0.74 g of copper (II) chloride dihydrate, 0.67 g of N,N,N',N'-tetramethylethylenediamine, and 87.0 g of methanol were added. Hereinafter, the contents in the reactor will be simply referred to as the "reaction liquid". Next, while stirring the reaction liquid at a stirring speed of 450 rpm, the temperature of the reaction liquid was raised to 50°C, and then air was blown in at 24 mL/min for 24 hours while maintaining the temperature of the reaction liquid at 50°C, to obtain a slurry-like solution. This slurry solution was filtered while being suspended and washed, and 17.9 g of white solid (1) was obtained as the filtrate.

When the obtained white solid (1) was analyzed by gas chromatography, it was found that the white solid (1) contained 88.6 GC area % of 3,3',5,5'-tetra-tert-butyl-6,6'-dimethyl-1,1'-biphenyl-2,2'-diol (the above-mentioned biphenol-a, hereinafter referred to as "biphenol-a") and 3.3 GC area % of compound A presumed to have a structure represented by the following formula (A).

<Separation of Compound A from White Solid (1)>
Compound A was separated from the resulting white solid (1) by the following procedure.
A tetrahydrofuran solution (39.9 g) was added to the obtained white solid (1) (17.9 g), and then the mixture was placed in a glass reaction vessel, and the temperature of the solution in the reaction vessel was raised to 60° C. while stirring at a stirring speed of 200 rpm using an oil bath, thereby dissolving the white solid (1). Next, 54 g of methanol was dropped into the reaction vessel at a dropping speed of 5 mL/min, and the stirring speed was reduced to 50 rpm, and the solution was cooled at a temperature decreasing rate of 0.8° C./min until the solution temperature in the reaction vessel reached 2° C., and further stirred for 2 hours to obtain a slurry-like solution.
The obtained slurry solution was filtered while being suspended in water, and the filtrate was collected. The obtained filtrate was analyzed by gas chromatography, and the filtrate contained 58.4 GC area % of biphenol-a and 12.7 GC area % of presumed compound A.

The resulting filtrate was dried, and then tetrahydrofuran (6.2 g) was added to the dried filtrate (2.9 g), which was then placed in a glass reaction vessel and heated to 60°C while stirring in an oil bath to dissolve the dried product. Methanol was then added dropwise, and the stirring speed was reduced and the solution in the reaction vessel was cooled to 2°C, yielding a slurry-like solution. The resulting slurry solution was filtered while being suspended and washed, and the filtrate was collected. The resulting filtrate was analyzed by gas chromatography and found to contain 27.6 GC area % biphenol-a and 19.6 GC area % estimated compound A.

The filtrate was dried to obtain 1.2 g of a white solid. The white solid (1.2 g) was dissolved in toluene (0.5 g), and then the solution was purified by open column purification using hexane/toluene = 100/1 as an eluent in a chromatography tube (inner diameter: 3.3 cm, silica gel packing length: 40 cm) packed with silica gel (product name: Wako Gel C-200, Fuji Film Wako Pure Chemical Industries, Ltd.), and the eluent from the chromatography tube was separated in 100 mL portions. When the eluent from the 17th tube was analyzed by gas chromatography, biphenol-a was not detected in the eluent, and the estimated compound A was contained in an amount of 70.7 GC area %. The eluent was concentrated using an evaporator, then dried under reduced pressure to obtain 0.06 g of a white solid (2) containing the estimated compound A.

<Isolation of Compound A from White Solid (2)>
About 6.4 mg of compound A was isolated from the obtained white solid (2) using liquid chromatography (LC method) under the following conditions.

The white solid (2) was dissolved in acetonitrile, and then an eluate containing Compound A was separated using preparative liquid chromatography (preparative LC) under the following preparative LC conditions.
Next, the separated eluate was concentrated using an evaporator and then dried under reduced pressure to obtain compound A.
(Preparative LC conditions)
Apparatus: LC-10A (apparatus name, manufactured by Shimadzu Corporation)
Preparative column: CAPCELLPAK C18 (product name, manufactured by Osaka Soda Co., Ltd., size: inner diameter 20 mm x length 150 mm, film thickness 5 μm)
Analysis temperature: 40°C
Eluent: acetonitrile Flow rate: 15 mL/min
Detector: UV detector (wavelength 210 nm)
Injection volume: 1000 μL per injection, performed 7 times

<Structural Identification of Compound A>
The isolated compound A was subjected to molecular weight measurement using the liquid chromatography mass spectrometry (LC/MS) and various NMR measurements ( ¹ H-NMR, ¹³ C-NMR, DEPT, HMQC, HMBC). The ¹ H-NMR spectrum of compound A is shown in Figure 1(a), and the ¹³ C-NMR spectrum is shown in Figure 1(b).
The analytical results of compound A were as follows:

(Molecular weight measurement results)
In liquid chromatography mass spectrometry (LC/MS), a positive mode of 494 ([M] ⁺ ) and a negative mode of 493 ([M−H] ⁻ ) were observed, and the molecular weight of compound A was determined to be 494.

( ^1H -NMR measurement results)
The peaks observed in the ¹ H-NMR spectrum were identified based on the structural formula represented by the following formula (α).
δ 0.77 (9H, s, signal 7 of formula (α)), δ 1.40 (9H, s, signal 2 of formula (α)), δ 1.43 (18H, s, signal 1 of formula (α) and 6 signals), δ 1.45 (6H, d, J = 5.95 Hz, 9 signals of formula (α), δ 1.89 (2H, dd, J = 14.4 Hz, 54.3 Hz, formula ( α) 8 signals ), δ 2.01 (3H, s, signal 10 of formula (α)), δ 2.02 (3H, s, signal 3 of formula (α)), δ 4.70 (1H, s, signal 10 of formula (α)), 5 signals of formula (α)), δ 4.81 (1H, s, 12 signals of formula (α)), δ 7.38 (1H, s, 4 signals of formula (α)), δ 7.41 (1H, s, 11 signals of formula (α)

( ^13C -NMR measurement results)
The peaks observed in the ¹³ C-NMR spectrum were identified based on the structural formula represented by the following formula (β).
δ 18.82 (signals of C and c in formula (β)), δ 29.65 (signal of B in formula (β)), δ 31.03, 31.14 (signal of i in formula (β)), δ 31. 53 (signal of f in formula (β)), δ 31.59 (signal of a in formula (β)), δ 31.69 (signal of A in formula (β)), δ 32.56 (signal of g in formula (β) ), δ 35.06 (signal of E in formula (β)), δ 35.91 (signal of d in formula (β)), δ 35.94 (signal of D in formula (β)), δ 39.17 ( δ 52.42 (signal of j in formula (β)), δ 52.42 (signal of h in formula (β)), δ 123.35 (signal of O in formula (β)), δ 123.37 (signal of o in formula (β)), δ 125.43 (signal of L in formula (β)), δ 126.73 (signal of formula (β) (signal of l in formula (β)), δ 131.32 (signal of k in formula (β)), δ 132.50 (signal of K in formula (β)), δ 133.94 (signal of N in formula (β)), δ 133. 97 (signal of n in formula (β)), δ 140.07 (signal of M in formula (β)), δ 140.30 (signal of m in formula (β)), 149.85 (signal of P in formula (β) (signal of p in formula (β)), 150.19 (signal of p in formula (β))

(DEPT measurement results)
It was ^confirmed that the signals of D, d, E, g, j, K, k, M, m, N, n, O, o, P, and p disappeared and the signal of h appeared in the opposite direction in the 13C-NMR spectrum.

(HMQC and HMBC measurement results)
The results of the HMQC and HMBC measurements are shown in Table 2 below.

From the above analytical results, it was confirmed that compound A obtained in Experimental Example 1 is a novel dihydroxybiphenyl compound having a bulky substituent in the ring structure and an asymmetric structure, as represented by the following formula (1A).

[Example 2: Production of the bisphosphite compound of the present invention (compound B)]
A tetrahydrofuran solution (12 mL) of compound A (1.08 g, 2.18 mmol) obtained in Example 1 was prepared and placed in a glass reactor, and while stirring at 0° C. under a nitrogen atmosphere, 0.466 g (5.067 mmol as sodium) of a commercially available metallic sodium mineral oil dispersion (product name: SD Super Fine ^™ (Sodium 25 wt% dispersion in mineral Oil), manufactured by Tokyo Chemical Industry Co., Ltd.) was added dropwise. Thereafter, the contents of the reactor were heated for 4 hours using an oil bath set at 65° C. to obtain a tetrahydrofuran solution containing the sodium form of compound A.
Next, a toluene solution (14 mL) of bisdiethylaminochlorophosphine (1.08 g, 5.126 mmol) was charged into a separately prepared glass reactor, and the obtained tetrahydrofuran solution containing the sodium form of compound A was added dropwise to the solution while stirring under a nitrogen atmosphere at a temperature of 0° C. After the dropwise addition, 12 mL of tetrahydrofuran contained in the content of the reactor was distilled off to obtain a toluene solution containing an aminophosphine form of compound A.

Then, the obtained toluene solution containing the aminophosphinated compound A was placed in a separately prepared glass reactor, and while stirring under a nitrogen atmosphere at 0°C, 6.03 g (27.25 mmol as hydrochloric acid gas) of a 1,4-dioxane hydrochloric acid solution (4 mol/L) was added dropwise, resulting in the formation of a precipitate of an amine hydrochloride. The precipitate was filtered off, and the filtrate was subjected to reduced pressure to remove excess hydrochloric acid gas and 1,4-dioxane, yielding a toluene solution containing a chlorophosphinated compound A.

Furthermore, a toluene solution containing the obtained chlorophosphine derivative of Compound A was stirred under a nitrogen atmosphere at 0°C, and a toluene solution (6.6 mL) of 1-naphthol (1.257 g, 8.72 mmol) and triethylamine (0.889 g, 8.78 mmol) was added dropwise thereto, and the mixture was allowed to stand at room temperature for three days, resulting in the formation of a precipitate of amine hydrochloride. The filtrate of the toluene solution obtained by filtering off the precipitate was washed three times with 50 mL of pure water, and the toluene phase was dehydrated using magnesium sulfate, after which the magnesium sulfate was filtered off using a filtration method. The toluene phase obtained after the dehydration process was then concentrated using an evaporator, and dried under reduced pressure to obtain 1.04 g of a white powder (3).

<Separation of Compound B from White Solid (3)>
The obtained white solid (3) (1.04 g) was dissolved in toluene (4 mL), and then purified by open column using hexane/toluene = 5/1 as an eluent in a chromatography tube (inner diameter: 3.3 cm, silica gel packing length: 30 cm) packed with silica gel (product name: Wako Gel C-200, Fuji Film Wako Pure Chemical Industries, Ltd.), and the eluent from the chromatography tube was separated in 100 mL portions. The eluents from the 16th to 22nd tubes were combined and analyzed by liquid chromatography, and the eluent contained compound B in an amount of 89.6 LC area %. The eluent was concentrated using an evaporator, and then dried under reduced pressure to obtain 0.63 g of a white solid (4) containing compound B.

<Isolation of Compound B from White Solid (4)>
Compound B was isolated from the obtained white solid (4) containing compound B by liquid chromatography (LC method) under the following conditions.

The white solid (4) was dissolved in acetonitrile, and then an eluate containing Compound B was separated using preparative liquid chromatography (preparative LC) under the following preparative LC conditions.
Next, the separated eluate was concentrated using an evaporator and then dried under reduced pressure to obtain compound B.
(Preparative LC conditions)
Apparatus: LC-10A (apparatus name, manufactured by Shimadzu Corporation)
Preparative column: CAPCELLPAK C18 (product name, manufactured by Osaka Soda Co., Ltd., size: inner diameter 20 mm x length 150 mm, film thickness 5 μm)
Analysis temperature: 40°C
Eluent: isopropanol/acetonitrile (20/80)
Flow rate: 15mL/min
Detector: UV detector (wavelength 290 nm)
Injection volume: 1000 μL/injection, 11 times

<Structural Identification of Compound B>
The isolated compound B was subjected to molecular weight and accurate mass measurement using a liquid chromatograph/time-of-flight mass spectrometer (LC/TofMS) and various NMR analyses ( ¹ H-NMR, ¹³ C-NMR, DEPT, HSQC, HMBC, ¹ H- ¹ H COSY). The ¹ H-NMR spectrum of compound B is shown in Figure 2(a) and ^{the 13} C-NMR spectrum is shown in Figure 2(b).
The analytical results of compound B were as follows:

(Results of molecular weight measurement and accurate mass measurement)
Using a liquid chromatograph/time-domain mass spectrometer (LC/ToFMS), an ion peak of m/z=1127.5507 ([M+H] ⁺ ) was observed in positive mode, and the molecular weight of compound B was determined to be 1127.5. In addition, the result of accurate mass measurement of this ion peak was 1127.5508, and the error from the theoretical value was within the range of −0.1 mDa and −0.1 ppm, so the composition formula of compound B was estimated to be C ₇₄ H ₈₀ O ₆ P ₂ .

( ¹ H-NMR measurement results (CDCl ₃ , TMS))
The peaks observed in the ¹ H-NMR spectrum were identified based on the structural formula represented by the following formula (γ).
δ 0.75 (9H, s, signal 6 of formula (γ)), δ 1.17 (18H, s, signals 1 and 5 of formula (γ)), δ 1.34 (3H, s, formula (γ) 8 signal of formula (γ)), δ 1.40 (9H, s, 2 signal of formula (γ)), δ 1.43 (2H, s, 8 signal of formula (γ)), δ 1.50 (1H, d, J = 14.9 Hz, signal 7 of formula (γ), δ 2.03 (3H, s, signal 3 of formula (γ) ), δ 2.10 (3H, s, signal 9 of formula (γ)), δ 2.71 (1H, d, J = 14.6 Hz, signal 7 of formula (γ)), δ 6.88 (1H, d, J = 7.80 Hz, 12 signals of formula (γ), δ 6.95 (1H, d, J = 7.96 Hz, 12 signals of formula (γ), δ 7.02 (1H, d, J = 7.80 Hz, 11 signals of formula (γ), δ 7.06-7.34 (14H, m, Signals 11, 12, 13, 15, and 16 of formula (γ), δ 7.38 (1H, d, J = 8.29, signal 13 of formula (γ), δ 7.51 (1H, s, δ 7.52 (1H, s, signal of formula (γ) 10), δ 7.58 (1H, d, J = 7.96, signal of formula (γ) 14) ), δ 7.61 (1H, d, J = 7.96, signal 14 of formula (γ)), δ 7.64 (1 H, d, J = 7.96, signal of 14), δ 7.65 (1H, d, J = 7.96, signal of 14 of formula (γ), δ 7.76 (1H, d, J = 8 .29, signal 17 of formula (γ), δ 7.82 (1H, d, J = 8.29, signal 17 of formula (γ), δ 7.84 (1H, d, J = 8.29 , signal 17 of formula (γ), δ 7.88 (1H, d, J = 8.29, signal 17 of formula (γ))

( ^13C -NMR measurement results)
The peaks observed in the ¹³ C-NMR spectrum were identified based on the structural formula represented by the following formula (ε).
δ 19.87, 19.91 (signal of C in formula (ε)), δ 19.94, 19.97 (signal of c in formula (ε)), δ 30.65 (signal of B in formula (ε)), 30.73 (signal of i in formula (ε)), δ 31.00 (signal of f in formula (ε)), δ 31.11 (signal of A in formula (ε)), δ 31.87 (signal of formula (ε) (signal of a in formula (ε)), δ 31.92 (signal of i in formula (ε)), δ 32.51 (signal of g in formula (ε)), δ 35.34 (signal of E in formula (ε)), δ 35. 81 (signal of d in formula (ε)), δ 35.88 (signal of D in formula (ε) (signal of j in formula (ε)), δ 39.73 (signal of j in formula (ε)), δ 53.25 (signal of h in formula (ε)), δ 112.99, δ 113.09, δ 113.26, δ 113.37, δ 113.46 , δ 113.56, δ 113.65, δ 113.74 (signal of R in formula (ε)), δ 122.45 (signal of Y and T in formula (ε)), δ 122.49 (signal of T in formula (ε) signal), δ 122.53 (signal of Y in formula (ε)), δ 122.61 (signals of Y and T in formula (ε)), δ 122.65 (signal of Y in formula (ε)), δ 124.86 , δ124.96, δ12 5.03, δ 125.08 (signal of X in formula (ε)), δ 125.10, δ 125.18, δ 125.23, δ 125.31 (signal of S in formula (ε)), δ 125.83, δ 125. 97, δ 126.04 (signal of W in formula (ε)), δ 126.26 (signal of l in formula (ε)), δ 126.52, 126.68, 126.82 (signal of Z in formula (ε) ), δ 127.08, δ 127.11, δ 127.18 (signal of V in formula (ε)), δ 127.52 (signal of L in formula (ε)), δ 131.72 (signal of o in formula (ε) ), δ 131. 87 (signal of O in formula (ε)), δ 134.46, δ 134.56, δ 134.60 (signal of U in formula (ε)), δ 135.71 (signal of n in formula (ε)), δ 135. 99 (signal of N in formula (ε)), δ 136.31 (signal of k in formula (ε)), δ 137.17 (signal of K in formula (ε)), δ 143.38 (signal of m in formula (ε) δ 143.57 (signal of M in formula (ε)), δ 148.13, δ 148.20 (signal of Q in formula (ε)), δ 149.73 (signal of p in formula (ε)), δ 149.81 (signal of P of formula (ε))

(DEPT measurement results)
It was confirmed that the signals D, E, g, j, K, k, M, m, N, n, O, o, P, p, Q, U, and Z in the ^13C -NMR spectrum disappeared, and the signal h appeared in the opposite direction.

(HMQ, CHMBC and ^1H - ^1H COSY measurement results)
The results of the measurements of HMQ, CHMBC and ¹ H- ¹ H COSY are shown in Table 3 below.

(IR measurement results, unit: cm ⁻¹ )
The IR measurement results were as follows:
567 (w), 594 (w), 702 (w), 729 (w), 766 (s), 793 (s), 872 (m), 891 (m), 906 (w), 1012 (s), 1026 (m), 1039 (m), 1078 (m), 1153 (w), 1169 (w), 1225 (s), 125 7(s), 1360(w), 1388(s), 1444(w), 1460(m), 1506(w), 1574(m), 1595(w), 1745(m), 2870(m), 2951(m), 3051(w)

From the above analysis results, it was confirmed that compound B obtained in Example 2 is a novel bisphosphite compound represented by the following formula (1B), which has a bulky substituent in the ring structure and an asymmetric structure.

[Example 3: Production of aldehyde]
Using the bisphosphite compound of the present invention, a hydroformylation reaction was carried out using propylene as a raw material in the following manner, and aldehyde production was evaluated.

After the inside of a 50 mL capacity stainless steel induction stirring autoclave was thoroughly dried, the inside of the autoclave was replaced with nitrogen three times.
In a separately prepared glass vessel, 4.84 mg (0.0179 mmol as Rh) of [Rh(OAc)(cod)] ₂ as an Rh source for the hydroformylation catalyst and 80.4 mg (0.0713 mmol, molar ratio of ligand L to Rh (L/Rh ratio)=4) of compound B, which is a bisphosphite compound of the present invention and was produced in Example 2, as a ligand for the hydroformylation catalyst were added under a nitrogen atmosphere, and further 14.0 mL (12.040 g) of toluene as a solvent and 1.0 mL (0.750 g) of n-dodecane as an internal standard substance for gas chromatography were added, followed by stirring to prepare a catalyst solution.

The catalyst solution was then injected into the autoclave using purified nitrogen gas, and the autoclave was then sealed. The concentration of the hydroformylation catalyst in the catalyst solution was 122 mg/L in terms of Rh.
The autoclave was replaced with nitrogen gas three times using nitrogen gas so that the internal pressure of the nitrogen gas was 2.0 MPaG, and then the nitrogen gas was released and 1.5 g of propylene gas was injected into the autoclave. Next, the reaction temperature in the autoclave was raised to 70° C., and oxo gas (H ₂ /CO=1/1, 0.6 MPaG as the oxo gas partial pressure at the beginning of the reaction) was injected so that the reaction pressure in the autoclave was 1.0 MPaG including the propylene pressure, and the hydroformylation reaction was carried out for 1.5 hours while maintaining this pressure and temperature. The oxo gas consumed in the hydroformylation reaction was automatically replenished from the pressure accumulator into the autoclave via the secondary pressure regulator, and the reaction was carried out so that the pressure in the autoclave was always maintained at 1.0 MPaG.

After the hydroformylation reaction was completed, the temperature inside the autoclave was cooled to room temperature (25° C.), and the gas phase and liquid phase recovered from the autoclave were subjected to component analysis by gas chromatography.
As a result of analysis, the reaction rate constant (k) was 2.8 h ^-1 , the total selectivity of n-butyraldehyde and i-butyraldehyde was 97.8%, and the molar ratio of n-butyraldehyde to i-butyraldehyde (n/i) was 75.1.

[Comparative Example 1: Production of aldehyde]
As a comparative example, a hydroformylation reaction was carried out using a symmetric bisphosphite compound having only a t-Bu group at the o-position of the phosphite substituent, and propylene as a raw material according to the following procedure, and the production of aldehyde was evaluated.

In Example 3, 80.4 mg of compound B was replaced with 76.4 mg of the phosphite ligand A (0.0713 mmol, ratio of ligand L to Rh = 4), but the hydroformylation reaction was carried out under the same conditions as in Example 3 to produce an aldehyde.

As a result of evaluation in the same manner as in Example 3, the reaction rate constant (k) was 2.8 h ⁻¹ , the total selectivity of n-butyraldehyde and i-butyraldehyde was 98.5%, and the molar ratio of n-butyraldehyde to i-butyraldehyde (n/i ratio) was 70.4.

[Examples 4-5 and Comparative Examples 2-3: Production of aldehydes]
A hydroformylation reaction was carried out under the same conditions as in Example 3, except that the type of the bisphosphite compound, the L/Rh ratio, the reaction temperature, the reaction pressure, and the reaction time were changed as shown in Table 4, to produce an aldehyde.
The results of evaluation performed in the same manner as in Example 3 are shown in Table 4.

[Example 6]
An aldehyde was produced by carrying out a hydroformylation reaction under the same conditions as in Example 3, except that compound B was changed to a mixture of compound B and phosphite ligand A (molar ratio: 50/50).
The results of evaluation performed in the same manner as in Example 3 are shown in Table 4.

The above evaluation results show that when the novel bisphosphite compound of the present invention is used as a ligand for a catalyst in a hydroformylation reaction, linear aldehydes can be efficiently produced while maintaining good reaction activity in the hydroformylation reaction.

(Thermal Stability Test)
The following thermal stability test was carried out to examine the thermal stability of the ligand assuming a series of steps in which the aldehyde produced after the hydroformylation reaction is separated by distillation and the catalyst liquid containing the ligand (bisphosphite compound) is recycled to the reactor.

[Example 7: Thermal stability test of the bisphosphite compound of the present invention]
The thermal stability of the bisphosphite compound of the present invention was evaluated according to the following procedure.

After the inside of a 100 mL capacity stainless steel induction stirring autoclave was thoroughly dried, the inside of the autoclave was replaced with nitrogen three times.
In a separately prepared glass vessel, under a nitrogen atmosphere, 40 mL of n-butylaldehyde (solvent), 18.0 mg (0.067 mmol as Rh) of [Rh(OAc)(cod)] ₂ as an Rh source for the hydroformylation catalyst, and 0.151 g (0.134 mmol, molar ratio of phosphorus atom in the ligand to Rh (P/Rh ratio)=2.01) of compound B produced in Example 2 as a ligand for the hydroformylation catalyst were prepared as a catalyst mixed solution. Next, the catalyst mixed solution was injected into the autoclave using purified nitrogen gas, and the autoclave was then sealed.

Next, while stirring the contents in the autoclave, oxo gas (H ₂ /CO = 1/1) was injected so that the internal pressure of the autoclave became 0.1 MPaG, and then the internal temperature of the autoclave was raised to 70°C and stirred for 30 minutes while maintaining this temperature.
The temperature inside the autoclave was then cooled to room temperature (25° C.), the oxo gas in the autoclave was purged, and an initial sample for analysis was taken from inside the autoclave under a nitrogen atmosphere. The inside of the autoclave was then replaced with nitrogen three times so that the internal pressure of the nitrogen gas was 0.5 MPaG, thereby replacing the oxo gas in the reaction solution and the oxo gas in the gas phase in the autoclave with nitrogen gas, and nitrogen gas was then injected into the autoclave so that the internal pressure was 0.1 MPaG.

Next, the temperature in the autoclave was raised to 130°C, and heating and stirring were performed while maintaining this temperature. After 88 hours, 183 hours, and 231 hours from when the temperature reached 130°C, the temperature in the autoclave was cooled to room temperature (25°C), the nitrogen gas in the autoclave was purged, and an analysis sample was taken from the autoclave under a nitrogen atmosphere. After taking the analysis sample, nitrogen gas was injected into the autoclave so that the internal pressure was 0.1 MPaG, and then the temperature in the autoclave was raised to 130°C, and heating and stirring were performed for a predetermined time while maintaining this temperature.
The obtained analytical sample was subjected to liquid chromatography under the liquid chromatogram measurement conditions described below to measure the decomposition rate of compound B. As a result, the decomposition rates of compound B after 88 hours, 183 hours, and 231 hours were 11.7 LC area %, 21.4 LC area %, and 26.6 LC area %, respectively.
The decomposition rate of compound B is the reduction rate (unit: area %) of the peak area of compound B in the liquid chromatogram of the sample obtained after 88 hours, 183 hours, and 231 hours, relative to the peak area of compound B in the liquid chromatogram of the initial sample.

(Liquid chromatogram measurement conditions)
High-performance liquid chromatogram measuring device: LC-20A (device name, manufactured by Shimadzu Corporation)
Degassing: Online degasser Analytical column: Inertsil ODS-2
Non-polar stationary phase (product name, column size: inner diameter 4.6 mm × column length: 250 mm, film thickness: 5 μm, manufactured by GL Sciences Inc.)
Column temperature: 40°C
Eluent: toluene:acetonitrile = 10:90 (weight ratio)
Eluent flow rate: 0.85 mL/min
Detector: UV-visible absorbance detector (detection wavelength: 290 nm)
Sample injection volume: 5 μL

[Comparative Example 4: Thermal Stability Test of Phosphite Ligand A]
As a comparative example, a symmetric bisphosphite compound having only a t-Bu group at the o-position of the phosphite substituent was subjected to a thermal stability evaluation according to the following procedure.

The thermal decomposition rate of the bisphosphite compound was evaluated under the same conditions as in Example 7, except that 0.151 g of compound B in Example 7 was changed to 0.143 g (0.134 mmol) of phosphite ligand A.
As a result, the decomposition rates of the bisphosphite compound after 88 hours, 183 hours and 231 hours were 14.3 LC area %, 30.9 LC area % and 39.0 LC area %, respectively.

The results of Example 7 and Comparative Example 4 are summarized in Table 5 below.

The above evaluation results show that a catalyst using the novel bisphosphite compound of the present invention as a catalytic ligand in a hydroformylation reaction has excellent thermal decomposition resistance. In processes that include an aldehyde distillation step exposed to heating conditions and a step of recycling the catalyst and catalytic ligand to the hydroformylation reaction, the bisphosphite compound of the present invention can exist stably, making it an industrially excellent ligand.

Although the present invention has been described in detail and with reference to specific embodiments, it will be apparent to those skilled in the art that various changes and modifications can be made therein without departing from the spirit and scope of the invention.
This application is based on Japanese Patent Application No. 2023-065067 filed on April 12, 2023 and Japanese Patent Application No. 2024-015052 filed on February 2, 2024, the entire contents of which are incorporated by reference.

According to the present invention, there can be provided a novel dihydroxybiphenyl compound having a bulky substituent in the ring structure and an asymmetric structure.
By using a catalyst in which the bisphosphite compound produced from the dihydroxybiphenyl compound of the present invention is used as a ligand together with a metal component, extremely excellent selectivity for linear aldehyde isomers can be obtained in the hydroformylation reaction.

Claims (27)

A dihydroxybiphenyl compound represented by the following general formula (1):

(In formula (1),
X is an alkylene group having 4 to 20 carbon atoms;
R ¹ and R ¹¹ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, and a cycloalkyl group having 3 to 20 carbon atoms, and R ¹ and X-R ¹¹ are different from each other.
R ² and R ¹² each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, an alkoxy group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, a cycloalkoxy group having 3 to 20 carbon atoms, a dialkylamino group having 2 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an aryloxy group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, an alkylaryloxy group having 7 to 20 carbon atoms, an arylalkyl group having 7 to 20 carbon atoms, an arylalkoxy group having 7 to 20 carbon atoms, a cyano group, a hydroxyl group, and a halogen atom;
R ³ and R ¹³ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, and an arylalkyl group having 7 to 20 carbon atoms;
^R4 and ^R14 each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms, an alkoxy group having 1 to 12 carbon atoms, a silyl group, a siloxy group, and a halogen atom. The dihydroxybiphenyl compound according to claim 1, wherein X is an alkylene group having 4 to 20 carbon atoms, including a quaternary carbon atom. The dihydroxybiphenyl compound according to claim 2, wherein X is an alkylene group having 4 to 5 carbon atoms, including a quaternary carbon atom. The dihydroxybiphenyl compound according to claim 3 , wherein X is an alkylene group having a structural unit represented by the following formula (1X):
-C( _CH3 ) ₂ - _CH2- (1X) R ¹ and R ¹¹ are each independently a tertiary alkyl group having 4 to 20 carbon atoms;
R ² and R ¹² are hydrogen atoms, R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 20 carbon atoms,
The dihydroxybiphenyl compound according to any one of claims 1 to 4, wherein R ⁴ and R ¹⁴ are each independently selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, an alkoxy group having 1 to 3 carbon atoms, and a halogen atom. R ¹ , R ¹¹ , R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 7 carbon atoms;
6. The dihydroxybiphenyl compound according to claim 5, wherein R ⁴ and R ¹⁴ are each independently an alkyl group having 1 to 3 carbon atoms. 7. The dihydroxybiphenyl compound according to claim 6, wherein R ¹ , R ¹¹ , R ³ and R ¹³ are t-butyl groups, and R ⁴ and R ¹⁴ are methyl groups. A bisphosphite compound represented by the following general formula (2):

(In formula (2),
X is an alkylene group having 4 to 20 carbon atoms;
R ¹ and R ¹¹ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, and a cycloalkyl group having 3 to 20 carbon atoms, and R ¹ and X-R ¹¹ are different from each other.
R ² and R ¹² each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, an alkoxy group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, a cycloalkoxy group having 3 to 20 carbon atoms, a dialkylamino group having 2 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an aryloxy group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, an alkylaryloxy group having 7 to 20 carbon atoms, an arylalkyl group having 7 to 20 carbon atoms, an arylalkoxy group having 7 to 20 carbon atoms, a cyano group, a hydroxyl group, and a halogen atom;
R ³ and R ¹³ each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, an alkylaryl group having 7 to 20 carbon atoms, and an arylalkyl group having 7 to 20 carbon atoms;
^R4 and ^R14 each independently represent a group selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group having 3 to 12 carbon atoms, an alkoxy group having 1 to 12 carbon atoms, a silyl group, a siloxy group, and a halogen atom.
Z ¹ to Z ⁴ each independently represent an aryl group having 6 to 20 carbon atoms, and may have a substituent, and the substituents may be bonded to each other to form a ^ring .
and Z ² , and Z ³ and Z ⁴ may not be bonded to each other, or may be bonded to each other to form a ring structure. The bisphosphite compound according to claim 8, wherein X is an alkylene group having 4 to 20 carbon atoms, including a quaternary carbon atom. The bisphosphite compound according to claim 9, wherein X is an alkylene group having 4 to 5 carbon atoms including a quaternary carbon atom. The bisphosphite compound according to claim 10, wherein the X is an alkylene group having a structural unit represented by the following formula (1X):
-C( _CH3 ) ₂ - _CH2- (1X) R ¹ and R ¹¹ are each independently a tertiary alkyl group having 4 to 20 carbon atoms;
R ² and R ¹² are hydrogen atoms, and R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 20 carbon atoms;
The bisphosphite compound according to any one of claims 8 to 11, wherein R ⁴ and R ¹⁴ are each independently selected from the group consisting of a hydrogen atom, an alkyl group having 1 to 3 carbon atoms, an alkoxy group having 1 to 3 carbon atoms, and a halogen atom. The bisphosphite compound according to any one of claims 8 to 11, wherein Z ¹ to Z ⁴ each independently have no substituent on an aromatic ring carbon atom adjacent to a carbon atom bonded to an oxygen atom, or have a substituent having 0 to 2 carbon atoms on the aromatic ring carbon atom. R ¹ , R ¹¹ , R ³ and R ¹³ are each independently a tertiary alkyl group having 4 to 7 carbon atoms;
The bisphosphite compound according to claim 12, wherein R ⁴ and R ¹⁴ are each independently an alkyl group having 1 to 3 carbon atoms. The bisphosphite compound according to any one of claims 8 to 11, wherein Z ¹ to Z ⁴ are each independently a 1-naphthyl group or a 2-naphthyl group. 15. The bisphosphite compound according to claim 14, wherein R ¹ , R ¹¹ , R ³ and R ¹³ are t-butyl groups, and R ⁴ and R ¹⁴ are methyl groups. A catalyst comprising a complex of the bisphosphite compound according to any one of claims 8 to 11 and a metal of Groups 8 to 10. The catalyst according to claim 17, wherein the molar ratio of the bisphosphite compound to the Group 8 to 10 metal is 0.00004 to 500. The catalyst according to claim 18, wherein the molar ratio of the bisphosphite compound to the Group 8 to 10 metal is 0.0002 to 100. The catalyst according to claim 19, wherein the molar ratio of the bisphosphite compound to the Group 8 to 10 metal is 0.001 to 50. A catalyst composition comprising a bisphosphite compound represented by the following general formula (3) and the bisphosphite compound according to any one of claims 8 to 11.

(In formula (3),
R ¹ , R ² and R ¹² , R ³ and R ¹³ , R ⁴ and R ¹⁴ , and Z ¹ to Z ⁴ are respectively defined as R ¹ , R ² and R ¹² , R ³ and R ¹³ , R ⁴ and R ¹⁴ , and Z ¹ to Z ⁴ in the general formula (2). The catalyst composition according to claim 21, in which the content of the bisphosphite compound represented by the general formula (3) is 80.0 mass% or more, and the content of the bisphosphite compound according to any one of claims 8 to 11 is 0.01 mass% or more. A method for producing an aldehyde by reacting an olefin compound with carbon monoxide and hydrogen in the presence of a Group 8 to 10 metal compound and a bisphosphite compound according to any one of claims 8 to 11. The method for producing an aldehyde according to claim 23, wherein the concentration of the Group 8 to 10 metal compound in the reaction solution is 0.05 to 5000 mg/L in terms of metal atoms. A method for producing an alcohol, comprising producing an aldehyde by the method for producing an aldehyde according to claim 23, and then reacting the aldehyde with hydrogen. A method for producing an aldehyde by reacting an olefin compound with carbon monoxide and hydrogen in the presence of the catalyst described in claim 17. A method for producing an alcohol, comprising producing an aldehyde by the method for producing an aldehyde according to claim 26 and then reacting the aldehyde with hydrogen.

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