Patent Application
20200290024
The present invention relates to a catalyst mixture which includes a catalyst used in a hydrogenation reaction of one or more nitro groups of an unsaturated cyclic compound (aromatic nitro compound) having a structure where one or more nitro groups are directly bonded the ring skeleton.
An aromatic halogen amine having a structure where one or more nitro groups and one or more amino groups are directly bonded as substituents to a ring skeleton of the same ring while separated from each other, is an important raw material of a medicine, a dye, an insecticide, a herbicide.
The aromatic halogen amine can be prepared, for example, by the hydrogenation reaction (catalytic hydrogenation reaction) of an aromatic halogen nitro compound having the corresponding chemical structure (aromatic nitro compound having a structure where one or more nitro groups and one or more halogen atoms are directly bonded as substituents to a ring skeleton of the same ring while separated from each other).
In this hydrogenation reaction, in addition to the reduction reaction (desired hydrogenation reaction) where the nitro group is reduced to an amino group, a reaction where a halogen atom is removed from the ring and replaced by a hydrogen atom (undesired side reaction. Hereinafter referred to as “dehalogenation reaction” as necessary) also happened. Hydrogen halide produced by the dehalogenation reaction corrodes the reaction vessel.
In general, it is known that the dehalogenation reaction of an aromatic halogen compound is accelerated under the condition that a noble metal catalyst such as Pt or Pd and a base (NaOH, KOH, NH4OH) coexist (for example, Non-Patent Documents 1 to 6). The reason why accelerating the dehalogenation reaction is that the base neutralizes the hydrogen halide generated by the dehalogenation reaction. This is described, for example, in Non-Patent Document 1, page 25, left column: Formulae (11) to (13) showing Liquid Phase Dechlorination Reaction, Non-Patent Document 3, page 98, left column: Formulae (1) to (3) showing Liquid Phase Dechlorination Reaction.
As explained above, in the hydrogenation reaction of the aromatic halogen nitro compound, it is important to sufficiently reduce the dehalogenation reaction and to selectively reduce the nitro group.
Various proposals have been made for selectively reducing the nitro group of the aromatic halogen nitro compound.
For example, in order to avoid the dehalogenation reaction, Patent Document 1 proposes that the hydrogenation reaction of the aromatic halogen nitro compound (an aromatic nitro derivative having a halogen atom bonded to an aromatic nucleus in Patent Document 1) is carried out in the presence of tungsten carbide and a strong acid (sulfuric acid, phosphoric acid, hydrochloric acid, hydrobromic acid).
Further, in order to selectively proceed the hydrogenation of a nitro group of the aromatic halogen nitro compound, Patent Document 2 proposes a noble metal catalyst in which Pt and Cu are finely dispersed on an activated carbon as a carrier in a predetermined supporting amount.
Furthermore, in order to selectively proceed the hydrogenation of a nitro group of the aromatic halogen nitro compound (for example, 1-nitro-3,4-dichlorobenzene, 4-nitrochlorobenzene), Patent Document 3 proposes a catalyst containing a Pt-supporting carbon and Fe oxide-supporting carbon (or Fe hydroxide supporting carbon).
Furthermore, in the hydrogenation reaction of a nitro group of the aromatic halogen nitro compound (4-chloro-2,5-dimethoxy-1-nitrobenzene), in order to isolate the reaction product 4-chloro-2,5-dimethoxyaniline without crystallization from the solvent (xylene), Patent Document 4 proposes a reaction system which includes a sulfurized Pt-supporting carbon catalyst, an aliphatic open chain amine (particularly morpholine), an alkaline aqueous solution {compound which gives a pH of 8 to 10 in an aqueous solution (for example, disodium borate, sodium formate, sodium acetate, sodium carbonate, disodium hydrogen phosphate, sodium hydroxide)}, a predetermined amount of water (30 mL in Example 1 of Patent Document 4, 1.5 mL of water contained in the catalyst), and a predetermined amount of an aromatic organic solvent (675 mL in Example 1 of Patent Document 4)
Incidentally, the present applicant submits, as publications where the above-mentioned publicly-known inventions are described, the following publications:
However, in the hydrogenation reaction of the aromatic halogen nitro compound, from the viewpoint of sufficiently reducing the dehalogenation reaction and selectively reducing the nitro group, the present inventors have found that there is still room for improvement even in the abovementioned conventional technique.
The present invention has been completed considering the abovementioned technical circumstances, and can provide a catalyst mixture which, in a nitro group hydrogenation reaction of an aromatic nitro compound having a structure in which nitro groups and halogen atoms are directly bonded as substituents to a ring skeleton of the same ring while separated from each other, is capable of selectively hydrogenating the nitro groups and sufficiently reducing the removal of the halogen atoms from the ring.
As the results of the present inventors' intensive study for solving the above problems, the present inventors have found that a structure of a catalyst mixture where a catalyst in which, in addition to Pt particles, Fe oxide particles are supported on a carrier is mixed with a predetermined base is effective, and then the present invention has been completed.
More specifically, the present invention is configured by the following technical elements.
Namely, the present invention provides:
(N1) a catalyst mixture comprising a catalyst which is used in a hydrogenation reaction of at least one among one or more nitro groups present in a reactant, which is an aromatic nitro compound having a structure in which one or more nitro groups and one or more halogen atoms are directly bonded as substituents to a ring skeleton of the same ring while separated from each other, which comprises:
a catalyst and a base, and
the catalyst comprises a support, and Pt particles and Fe oxide particles supported on the support, and
the base has a basicity stronger than at least one aromatic amine obtained as a product from the hydrogenation reaction and having one or more amino groups.
In carrying out the selective hydrogenation reaction of the nitro group of the aromatic halogen nitro compound, despite the general recognition of those skilled in the art that addition of a base in this chemical system promotes the dehalogenation reaction as described in the aforementioned Non-Patent Documents 1 to 6, the present inventors have intentionally tried to add a base in a chemical system of a catalyst in which Pt particles and Fe oxide particles coexist, which have not been attempted in the past. As a result, though the detailed mechanism has not been found, in the hydrogenation reaction of the nitro group of the aromatic halogen nitro compound, the catalyst mixture satisfying the above configuration can selectively hydrogenate the nitro group, and the removal of the halogen atom from the ring can be sufficiently reduced.
In the present invention, the “basic” when comparing the basicity between a base and a product (at least one of aromatic amines having one or more amino groups) means “pKa (=−log Ka)”. Here, “Ka” represents a concentration acid dissociation constant. In the present invention, the “state in which the base has a basicity stronger than the product” means that “the pKa of the base is larger than the pKa of the product”. Further, when comparing the pKa of the base with the product pKa, it is not necessary to use the base pKa and the product pKa as measured in the actual reaction system. For comparison of the pKa, the Ka and pKa of each compound defined and described in “Revised 5th Edition Chemical Handbook Basic II (edited by The Chemical Society of Japan)”, or the Ka and pKa of each compound described in the stability constant database summarized by the V6 Committee of IUPAC (L. D. Pettit, K. J. Powell, “Stability Constants Database”, Academic Software (1997)).
From the viewpoint of obtaining the effect of the present invention more reliably, in the catalyst mixture of the present invention described in (N1), it is preferable that
(N2) the base and a component of a solvent used in the hydrogenation reaction satisfy the condition of the following equation (1):
0.90≤{1000×(B/Vs)}≤190.00 (1)
in the equation (1), B being a substance amount (mol) of the base, and Vs being a volume (L) of the organic solvent.
When adjusting an amount of the base contained in the catalyst mixture within the range which satisfies the condition of the above formula (1) with respect to a volume of the organic solvent in the reaction system where the catalyst mixture is used, the effect of the present invention can be more reliably obtained.
Further, from the viewpoint of obtaining the effect of the present invention more reliably, in the catalyst mixture of the present invention described in (N1) or (N2), it is preferable that
(N3) the base and the reactant used in the hydrogenation reaction satisfy the condition of the following equation (2):
0.35%≤{100×(B/R)}≤75.50% (2)
in the equation (2), B being a substance amount (mol) of the base, and R being a substance amount (mol) of the reactant.
When adjusting an amount of the base contained in the catalyst mixture within the range which satisfies the condition of the above formula (1) with respect to a substance amount of the reactant in the reaction system where the catalyst mixture is used, the effect of the present invention can be more reliably obtained.
Further, from the viewpoint of obtaining the effect of the present invention more reliably, in the catalyst mixture of the present invention described in any one of (N1) to (N3), it is preferable that
(N4) a component of a solvent used in the hydrogenation reaction satisfies the condition of the following equation (3):
0.00%≤{100×(Vh/Vs)}≤30.00% (3)
in the equation (3), Vh being a volume (L) of an introduced water other than the yielded water, and Vs being a volume (L) of the organic solvent.
The present inventors have found that by setting the water content in the reaction system where the catalyst mixture of the present invention is used to be relatively small as mentioned above, the catalyst mixture of the present invention can exhibit the effect of reducing the dehalogenation reaction more reliably. This structure is different from the catalyst described in Patent Document 4 (catalyst having a structure where the Fe oxide is not contained and used in a reaction system where contains water), and shows a remarkable effect obtained through the investigation by the present inventors.
Furthermore, from the same viewpoint, in a case of the catalyst mixture (N4), it is more preferable that
(N5) the water satisfies the condition of the following equation (4):
1.00%≤{100×(Vh/Vs)}≤5.00% (4)
Further, any one of the catalyst mixtures of any one of (N1) to (N5) may further contain
(N6) a dehydrating agent.
When previously mixing the dehydrating agent, the water content can be reduced in the reaction system where the catalyst mixture is used, and there is a case where the effects of the present invention can be obtained easily.
The present invention can provide the catalyst mixture which, in a nitro group hydrogenation reaction of an aromatic nitro compound (aromatic halogen nitro compound) having a structure in which nitro groups and halogen atoms are directly bonded as substituents to a ring skeleton of the same ring while separated from each other, is capable of selectively hydrogenating the nitro groups and sufficiently reducing the removal of the halogen atoms from the ring.
In the following, preferred embodiments of the present invention are explained in detail.
The catalyst mixture of the present embodiment contains the catalyst and the base. The catalyst contains the support, and the Pt particles and the Fe oxide particles supported on the support. The base has a basicity stronger than at least one aromatic amine obtained as the product from the hydrogenation reaction and having one or more amino groups.
The catalyst is not particularly limited as long as the catalyst contains the support, and the Pt particles and the Fe oxide particles supported on the support.
The support of the catalyst is not particularly limited as long as the support can support the Pt particles and the Fe oxide particles and has a large surface area. Examples include a carbon-based material such as an activated carbon, a pulverized activated carbon, a grassy carbon (GC), a fine carbon, a carbon black, graphite, or a carbon fiber, or a glass-based or a ceramic-based material such as an oxide, and may be properly used.
The specific surface area of the support is preferably 500 m3/g or more, more preferably 800 m3/g or more, and still more preferably 1000 m3/g or more.
In the Fe oxide particles of the catalyst contained in the catalyst mixture, the Fe oxide is not particularly limited, but preferably contains Fe2O3 as a main component.
The base contained in the catalyst mixture is not particularly limited as long as the base has a basicity stronger than at least one of the aromatic amines having one or more amino groups obtained as the product by hydrogenation reaction, and, in the state of being mixed with the Pt particles and the Fe oxide particles, has stability such that the chemical reaction dose not proceed with these particles at normal temperature and normal pressure. Any of inorganic base and organic base can be used. Further, the base can be properly used in consideration of the combination with the reactant and the solvent in the reaction system to be used. From the viewpoint of availability and the like, preferable examples of the base include sodium carbonate, sodium bicarbonate, potassium carbonate, triethylamine, sodium acetate.
The “aromatic amine having one or more amino groups” desirably is the aromatic halogen amine as the main product, but within the range where the effect of the present invention can be obtained (within the range being allowable in the reaction system to be used), a case where an aromatic amine which is a dehalogenated body is slightly contained may be allowable.
The content of the base contained in the catalyst mixture may be set to an optimum value in the reaction system and reaction conditions where the catalyst mixture is used.
However, as mentioned above, from the viewpoint of obtaining the effect of the present invention more reliably, in the catalyst mixture, it is preferable that the base and a component of a solvent used in the hydrogenation reaction satisfy the condition of the following equation (1):
0.90≤{1000×(B/Vs)}≤190.00 (1)
in the equation (1), B being a substance amount (mol) of the base, and Vs being a volume (L) of the organic solvent.
Further, from the viewpoint of obtaining the effect of the present invention more reliably, in the catalyst mixture, it is preferable that the base and the reactant used in the hydrogenation reaction satisfy the condition of the following equation (2):
0.35%≤{100×(B/R)}≤75.50% (2)
in the equation (2), B being a substance amount (mol) of the base, and R being a substance amount (mol) of the reactant.
Further, from the viewpoint of obtaining the effect of the present invention more reliably, in the catalyst mixture, it is preferable that a component of a solvent used in the hydrogenation reaction satisfies the condition of the following equation (3):
0.00%≤{100×(Vh/Vs)}≤30.00% (3)
in the equation (3), Vh being a volume (L) of an introduced water other than the yielded water, and Vs being a volume (L) of the organic solvent.
Furthermore, from the same viewpoint, in this case, it is more preferable that the water satisfies the condition of the following equation (4):
1.00%≤{100×(Vh/Vs)}≤5.00% (4)
Further, the catalyst mixture may further contain the dehydrating agent.
The dehydrating agent is not particularly limited as long as, in the state of being mixed with the Pt particles and the Fe oxide particles, the agent has stability such that the chemical reaction does not proceed with these substances at normal temperature and normal pressure. From the viewpoint of availability and the like, preferable examples of the dehydrating agent include zeolite, sodium sulfate, magnesium sulfate.
The solvent of the reaction system where the catalyst mixture is used is not particularly limited as long as the solvent has chemical properties capable of dissolving at least a part of the reactant (aromatic halogen nitro compound). Preferred examples include toluene, xylene, benzene, chlorobenzene, dichlorobenzene, and an alcohol having 1 to 3 carbon atoms. A mixture thereof at an optional ratio may be used.
The reactant (aromatic halogen nitro compound) in the reaction system where the catalyst mixture is used is not particularly limited, and it is preferable that the reactant has the structure represented by the following general formula (C1):
In the formula (C1),
n represents an integer of 1 or more,
m represents an integer of 1 or more,
α represents an integer of 0 or more,
β represents an integer of 0 or more, and
5≤(n+m+α+β)≤6,
R represents hydrogen atom, amino group, hydroxyl group or a mono-valent or more-valent organic group having at least one carbon atom,
X represents any one of halogen atoms,
Y represents, in the case of α=1, an atom of C, N, O, or S, and, in the case of α≥2, at least two atoms selected from the group consisting of C, N, O and S,
Z represents, in the case of β=1, an atom of C, N, O, or S, and, in the case of β≥2, at least two atoms selected from the group consisting of C, N, O and S, and
Y and Z may be the same or different from each other.
Here, when α is 2 or more, R may be a divalent organic group bonded to two adjacent Y atoms. In this case, the aromatic nitro compound may have a structure of a condensed ring compound.
In addition, R which is an organic group having mono- or more-valence, may have a structure in which the moiety bonding to Yα is represented by “—O—” or “—S—”.
For example, in the formula (C1), in the case of α=2, Y1=C, Y2=N, R=H, β=2, Z1=C, Z2=C, m=1, X=Br, n=1, (n+m+α+β)=6, (C1) is 2-bromo-5-nitropyridine represented by the following formula (C1-1).
The reactant (aromatic halogen nitro compound) in the reaction system where the catalyst mixture is used may have the structure represented by the following general formula (C2):
In the formula (C2),
n represents an integer of 1 or more,
m represents an integer of 1 or more,
α represents an integer of 0 or more,
β represents an integer of 0 or more, and
5≤(n+m+α+β)≤6,
R represents hydrogen atom, amino group, hydroxyl group or a mono-valent or more-valent organic group having at least one carbon atom,
X represents any one of halogen atoms,
Y represents, in the case of α=1, an atom of C, N, O, or S, and, in the case of α≥2, at least two atoms selected from the group consisting of C, N, O and S,
Z represents, in the case of β=1, an atom of C, N, O, or S, and, in the case of β≥2, at least two atoms selected from the group consisting of C, N, O and S,
Y and Z may be the same or different from each other, and
J represents a divalent organic group having one or more carbon atoms, and in the case of m≥2, J may be the same or different from each other.
In addition, R which is an organic group having mono- or more-valence, may have a structure in which the moiety bonding to Yα is represented by “—O—” or “—S—”.
For example, in the formula (C2), the moiety represented by the “X-J-” may have the following structures represented by the formulae (C2-1), (C2-2), (C2-3), and (C2-4).
X—C—(C=O)—N— (C2-1)
X—C═C—C— (C2-2)
X—C—C— (C2-3)
In the formula (C2-4), X1 and X2 each represent any one of halogen atoms, and X1 and X2 may be the same or different from each other.
The preparation process of the catalyst mixture is not particularly limited, and any combination of known processes can be employed.
As the catalyst contained in the catalyst mixture, for example, a catalyst where the Pt particles and the Fe oxide particles are supported on the support may be obtained by subjecting a dispersion containing a Pt compound, a Fe compound and water to reduction treatment to the support. The supporting of Pt and the supporting of Fe oxide may be carried out at the same time as described above, or one may be carried out first and then the other may be later.
The mixing procedure of the catalyst and the base is also not particularly limited as long as these components can sufficiently mix without causing any undesired chemical reaction.
Further, the mixing procedure of the catalyst, the base and the dehydrating agent is also not particularly limited as long as these components can sufficiently mix without causing any undesired chemical reaction. The order of mixing of the catalyst, the base and the dehydrating agent may be properly set by considering the respective chemical properties or the like.
Furthermore, the catalyst mixture may be solid or liquid. When being solid, it may be powder.
In the following, the present invention is explained in detail by referring working examples, but the present invention is not limited by the following working examples.
As the catalyst, a catalyst where the Pt particles and the Fe oxide particles were carried on a carbon support {trade name “NE-01M02”, content of Pt: 1.0 wt %, content of Fe: 0.20 wt % available from N. E. CHEMCAT Co. (hereinafter referred to as “Pt-FeOx/C” as necessary)} was prepared.
In the Pt-FeOx/C, the carbon support is an activated carbon (specific surface area based on BET measurement is 900: m2/g), and the Fe oxide particles are Fe2O3 as a main component (Fe2O3 is approximately 100% based on XPS analysis).
As the base, a commercially available Na2CO3 was prepared.
A catalyst mixture was obtained by mixing 127.0 mg (water content: 0.141 mL) of Pt-FeOx/C powder and 1.0 mg of Na2CO3.
The catalyst mixtures of Example 2 to Example 5 were prepared in the same preparation conditions and the same raw materials as Example 1 except that the amount of Na2CO3 was changed to the value shown in Table 1.
The catalyst mixture of Example 6 was prepared in the same preparation conditions and the same raw materials as in Example 1 except that 20 mg of a commercially available K2CO3 was used instead of the amount of Na2CO3.
The catalyst mixture of Example 7 was prepared in the same preparation conditions and the same raw materials as in Example 1 except that 72.6 mg of a commercially available (CH3CH2)3N was used instead of the amount of Na2CO3.
The catalyst mixtures of Example 8 to Example 14 were prepared in the same preparation conditions and the same raw materials as Example 3 except that the volume Vh (mL) of water was changed to the value shown in Table 1.
As the catalyst of Comparative Example 1, the catalyst consisting of the powder of Pt-FeOx/C which was the same as that in Example 1 was prepared without using a base.
The catalyst mixture of Comparative Example 2 was prepared in the same preparation conditions and the same raw materials as in Comparative Example 1 except that 200 mg of a commercially available NaCl was used without using a base.
The catalyst mixture of Comparative Example 3 was prepared in the same preparation conditions and the same raw materials as in Comparative Example 2 except that 30 mg of a commercially available Na2SO4 was used without using a base.
Instead of the Pt-FeOx/C used in Example 1, as the catalyst, a catalyst where the Pt particles were carried on a carbon support {trade name “NE-01M00”, content of Pt: 1.0 wt %, available from N. E. CHEMCAT Co. (hereinafter referred to as “Pt/C” as necessary)} was prepared.
In the Pt/C, the carbon support is an activated carbon (specific surface area based on BET measurement is 900: m2/g).
As the base, a commercially available Na2CO3 was prepared.
A catalyst mixture was obtained by mixing 127.0 mg (water content: 0.113 mL) of Pt/C powder and 10.0 mg of Na2CO3.
The catalyst mixture of Comparative Example 2 was prepared in the same preparation conditions and the same raw materials as Comparative Example 1 except that the amount of Na2CO3 was changed to the value shown in Table 1.
The catalyst mixtures of Comparative Example 6 to Comparative Example 8 were prepared in the same preparation conditions and the same raw materials as Comparative Example 1 except that the amount of the Pt/C powder to be used was changed to 140.0 mg (water content: 0.123 mL).
As the catalyst of Comparative Example 9, the catalyst consisting of the powder of Pt/C which was the same as that in Comparative Example 1 was prepared without using a base.
The hydrogenation reaction (hydrogenation reaction of nitro group) represented by the following reaction scheme (C1-11) was achieved by using the catalyst mixtures of Example 1 to Example 14 and Comparative Example 1 to Comparative Example 9.
Here, in the hydrogenation reaction represented by the reaction scheme (C1-11), 2-bromo-5-nitropyridine represented by the formula (C1-1) has a heterocyclic structure having an N atom. Compared to 2-bromo-5-nitrobenzene which has a structure in which the N atom in this heterocyclic ring is replaced with a C atom, 2-bromo-5-nitropyridine is a reactant which promotes not only the main hydrogenation reaction of the nitro group (main product being 5-amino-2-bromopyridine represented by the formula (C1-2)), but also promotes easily the side reaction of the debromination reaction (by-product being 3-aminopyridine represented by the formula (C1-3).
Reactant: 2.5 mmol of 2-Bromo-5-nitrobenzene represented by the formula (C1-1)
Solvent: 10 mL of toluene
Pressure of hydrogen: 0.6 MPa
Reaction temperature: 50° C.
Reaction time: 5 hours
In the hydrogenation reaction where the catalyst mixtures of Comparative Example 6 to Comparative Example 8 were used, water was added to each reaction system. The amount of water added to the reaction composition of Comparative Example 6 was adjusted to 0.444 mL, and the amount of water added to the catalyst mixtures of Comparative Example 7 and Comparative Example 8 were adjusted to be 1.000 mL.
The results obtained for the catalyst mixtures of Examples 1 to 14 and Comparative Examples 1 to 9 are shown in Table 1 and Table 2. The formula weight of Na2CO3 was 106 g mol, the formula weight of K2CO3 was 138.2 g mol, and the formula weight of (CH3CH2)3N was 101 g mol.
From the results shown in Table 2, when the reaction system using the catalyst mixtures of Example 1 to Example 14 which satisfies the constitution of the present invention was compared with the reaction system using the catalyst mixtures of Comparative Example 1 to Comparative Example 9, it has been clear that the debromination reaction to 3-aminopyridine represented by the formula (C1-3) was sufficiently reduced, and the selectivity of the desired 5-amino-2-bromopyridine represented by the formula (C1-2) was improved.
In particular, when the reaction system using the catalyst mixtures of Example 1 to Example 14 which satisfies the constitution of the present invention was compared with the reaction system using the catalyst mixture of Comparative Example 1 which has the structure similar to that of Patent Document 3 described as a prior art document (reaction system which has a catalyst containing a Pt component and an iron oxide component, and does not contain a base), it has been clear that the debromination reaction to 3-aminopyridine represented by the formula (C1-3) was sufficiently reduced.
Further, when the reaction system using the catalyst mixtures of Example 1 to Example 14 which satisfies the constitution of the present invention was compared with the reaction system using the catalyst mixture of Comparative Example 6 which has the structure similar to that of Patent Document 4 described as a prior art document (reaction system which has a catalyst containing a Pt component, and a base and water is added (in Example 1 of Patent Document 4, 100×(Vh/Vs)=100×(amount of added water 30 mL+water contained in the catalyst 1.5 mL)/toluene 675 mL=4.6%), it has been clear that the debromination reaction to 3-aminopyridine represented by the formula (C1-3) was sufficiently reduced.
From the aforementioned results, it has been clear that, in a nitro group hydrogenation reaction of an aromatic nitro compound (aromatic halogen nitro compound) having a structure in which nitro groups and halogen atoms are directly bonded as substituents to a ring skeleton of the same ring while separated from each other, the catalyst mixture of the present examples is capable of selectively hydrogenating the nitro groups and sufficiently reducing the removal of the halogen atoms from the ring.
The catalyst mixture of the present invention has the catalyst activities that, in a nitro group hydrogenation reaction of an aromatic nitro compound (aromatic halogen nitro compound) having a structure in which nitro groups and halogen atoms are directly bonded as substituents to a ring skeleton of the same ring while separated from each other, is capable of selectively hydrogenating the nitro groups and sufficiently reducing the removal of the halogen atoms from the ring.
Therefore, the present invention contributes to the development of efficient mass production technology of the aromatic halogen amine which is an important raw material of medicines, dyes, insecticides and herbicides, and further contributes to the development of the industries of pharmaceuticals, dyes, insecticides, herbicides.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2016-058059 | Mar 2016 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2017/005582 | 2/15/2017 | WO | 00 |
