WO2017163681A1 - 反応組成物及びこれを用いた反応システム - Google Patents
反応組成物及びこれを用いた反応システム Download PDFInfo
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- WO2017163681A1 WO2017163681A1 PCT/JP2017/005584 JP2017005584W WO2017163681A1 WO 2017163681 A1 WO2017163681 A1 WO 2017163681A1 JP 2017005584 W JP2017005584 W JP 2017005584W WO 2017163681 A1 WO2017163681 A1 WO 2017163681A1
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D213/00—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
- C07D213/02—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
- C07D213/04—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom
- C07D213/60—Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen or carbon atoms directly attached to the ring nitrogen atom with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D213/72—Nitrogen atoms
- C07D213/73—Unsubstituted amino or imino radicals
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/8906—Iron and noble metals
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/20—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
- B01J35/27—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a liquid or molten state
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2235/00—Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties
Definitions
- the present invention relates to a reaction composition containing a catalyst and an organic solvent, and a reaction system using the same. More specifically, the present invention relates to a catalyst and an organic solvent used in a hydrogenation reaction of an unsaturated cyclic compound (aromatic nitro compound) having a structure in which one or more nitro groups are directly bonded to a ring skeleton. And a reaction composition comprising: In addition, the present invention uses the reaction composition of the present invention to selectively hydrogenate the nitro group of the aromatic nitro compound, which is a reactant, and to sufficiently reduce elimination of halogen atoms from the ring. The present invention relates to a reaction system capable of realizing a reaction.
- Aromatic halogenamines having a structure in which one or more nitro groups and one or more amino groups are directly bonded as substituents to the same ring skeleton are used as pharmaceuticals, dyes, insecticides and herbicides. It is an important raw material.
- This aromatic halogenamine is, for example, an aromatic halogen nitro compound having a chemical structure corresponding to the aromatic halogenamine (a state in which one or more nitro groups and one or more halogen atoms are separated into ring skeletons of the same ring as substituents, respectively) Can be produced by a hydrogenation reaction (catalytic hydrogenation reaction).
- Patent Document 1 discloses a hydrogenation reaction of an aromatic halogen nitro compound (in Patent Document 1, “aromatic nitro derivative having a halogen atom bonded to an aromatic nucleus”) with the intention of avoiding a dehalogenation reaction.
- aromatic halogen nitro compound in Patent Document 1, “aromatic nitro derivative having a halogen atom bonded to an aromatic nucleus”
- Patent Document 2 discloses that activated carbon is finely loaded on activated carbon as a carrier with a predetermined amount of Pt and Cu, with the intention of allowing selective hydrogenation of the nitro group of the aromatic halogen nitro compound.
- Noble metal catalysts distributed in the region have been proposed.
- Patent Document 3 the hydrogenation of a nitro group of an aromatic halogen nitro compound (for example, 1-nitro-3,4-dichlorobenzene, 4-nitrochlorobenzene) is intended to proceed selectively,
- a catalyst containing Pt-supported carbon and Fe oxide-supported carbon (or Fe hydroxide-supported carbon) has been proposed.
- Patent Document 4 discloses the product 4-chloro-2,5-dimethoxyaniline in the hydrogenation reaction of the nitro group of an aromatic halogen nitro compound (4-chloro-2,5-dimethoxy-1-nitrobenzene). Intended to be isolated from a solvent (xylene) without crystallization, a sulfite-supported Pt-supported carbon catalyst, an aliphatic open-chain amine (especially morpholine), an alkaline aqueous solution ⁇ in aqueous solution a compound giving a pH of 8 to 10 (for example, disodium borate, sodium formate, sodium acetate, sodium carbonate, disodium hydrogen phosphate, sodium hydroxide) ⁇ and a predetermined amount of water (30 mL in Example 1 of Patent Document 4) And a reaction system containing a predetermined amount of an aromatic organic solvent (675 mL in Example 1 of Patent Document 4). It has been proposed.
- a solvent xylene
- the present invention has been made in view of such technical circumstances, and is an aromatic nitro compound having a structure in which a nitro group and a halogen atom are directly bonded to each other as a substituent in a ring skeleton of the same ring. It is an object of the present invention to provide a reaction composition that can selectively hydrogenate a nitro group and sufficiently reduce elimination of a halogen atom from a ring.
- the inventors of the present invention have a configuration of a reaction composition having a catalyst in which Fe oxide particles are supported on a carrier in addition to Pt particles, and a predetermined organic solvent. Has been found to be effective, and the present invention has been completed.
- the present invention includes the following technical matters. That is, the present invention (N1) 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 in a ring skeleton of the same ring is used as a reactant, A catalyst used in a hydrogenation reaction to convert at least one of the nitro groups to an amino group; A solvent, Contains The catalyst includes a support, Pt particles and Fe oxide particles supported on the support, The constituent components of the solvent satisfy the condition of the following formula (1). Reaction composition.
- Vh represents the volume (L) of water introduced in addition to the reaction product water
- Vs represents the volume (L) of an organic solvent capable of dissolving at least a part of the reaction product.
- the present inventors In carrying out the selective hydrogenation reaction of the nitro group of the aromatic halogen nitro compound, the present inventors compared the moisture content as described above in the catalyst chemical system in which Pt particles and Fe oxide particles coexist. However, the detailed mechanism has not been elucidated, but the reaction composition satisfying the above configuration can selectively hydrogenate the nitro group in the hydrogenation reaction of the nitro group of the aromatic halogen nitro compound. The inventors have found that elimination of halogen atoms from the ring can be sufficiently reduced.
- reaction composition of the present invention described in (N1) is a reactant.
- reaction composition of the present invention described in (N2) is a reactant.
- An aromatic nitro compound may be further contained.
- reaction composition of the present invention described in (N2) is (N3)
- An aromatic amine having at least one amino group obtained as a product by a hydrogenation reaction of an aromatic nitro compound may be further included.
- reaction composition of the present invention according to any one of (N1) to (N3) (N4) It is more preferable that the constituent components of the solvent further satisfy the condition of the following formula (2). 1.00% ⁇ ⁇ 100 ⁇ (Vh / Vs) ⁇ ⁇ 5.00% (2)
- reaction composition of any one of (N1) to (N4) is (N5)
- a dehydrating agent may further be included.
- the amount of water in the reaction composition of the present invention can be reduced, and the effects of the present invention can be easily obtained.
- the present invention also provides a reaction system including a reaction vessel that can contain the reaction composition according to any one of (N1) to (N6) as a reactant.
- the reaction system of the present invention uses the reaction composition of the present invention, the nitro group of the aromatic nitro compound that is the reactant can be selectively hydrogenated, and the elimination of halogen atoms from the ring can be sufficiently reduced. Hydrogenation reaction can be realized.
- the hydrogen of a nitro group of an aromatic nitro compound (aromatic halogen nitro compound) having a structure in which a nitro group and a halogen atom are directly bonded as substituents to the ring skeleton of the same ring.
- aromatic nitro compound aromatic halogen nitro compound
- a reaction composition that can selectively hydrogenate a nitro group and sufficiently reduce elimination of a halogen atom from a ring is provided.
- a system can be provided.
- the reaction composition of this embodiment contains a catalyst and a solvent.
- the catalyst includes a support, Pt particles supported on the support, and Fe oxide particles.
- the organic solvent has a chemical property that can dissolve at least a part of the reactant.
- the catalyst contained in the reaction composition is not particularly limited as long as it contains a support, Pt particles and Fe oxide particles supported on the support.
- the catalyst carrier is not particularly limited as long as it can support Pt particles and Fe oxide particles and has a large surface area. It can be suitably selected from carbon materials such as activated carbon, pulverized activated carbon, glassy carbon (GC), fine carbon, carbon black, graphite, and carbon fiber, and glass or ceramic materials such as oxides.
- carbon materials such as activated carbon, pulverized activated carbon, glassy carbon (GC), fine carbon, carbon black, graphite, and carbon fiber, and glass or ceramic materials such as oxides.
- the specific surface area of the carrier is preferably 500 m 3 / g or more, more preferably 800 m 3 / g or more, and still more preferably 1000 m 3 / g or more.
- the Fe oxide is not particularly limited, but it is preferable that Fe 2 O 3 is the main component.
- the component of the solvent is prepared so as to satisfy the condition of the following formula (1). 0.00% ⁇ ⁇ 100 ⁇ (Vh / Vs) ⁇ ⁇ 10.00% (1)
- Vh represents the volume (L) of water introduced in addition to the reaction product water
- Vs represents the volume (L) of an organic solvent capable of dissolving at least a part of the reaction product.
- the constituent components of the solvent further satisfy the condition of the following formula (2). 1.00% ⁇ ⁇ 100 ⁇ (Vh / Vs) ⁇ ⁇ 5.00% (2)
- the reaction composition may further contain a dehydrating agent.
- the dehydrating agent is not particularly limited as long as it has a stability that does not cause a chemical reaction with these at normal temperature and normal pressure in a state where it is mixed with Pt particles and Fe oxide particles.
- preferred examples of the dehydrating agent include zeolite, sodium sulfate, and magnesium sulfate from the viewpoint of availability.
- the organic solvent contained in the reaction composition is not particularly limited as long as it has chemical properties capable of dissolving at least a part of the reactant (aromatic halogen nitro compound).
- the reactant aromatic halogen nitro compound
- toluene, xylene, benzene, chlorobenzene, dichlorobenzene, and alcohol having 1 to 3 carbon atoms are preferable. You may employ
- the reactant (aromatic halogen nitro compound) in the reaction system in which the reaction composition is used is not particularly limited, but preferably has a structure represented by the following general formula (C1).
- n represents an integer of 1 or more
- m represents an integer of 1 or more
- ⁇ represents an integer of 0 or more
- ⁇ represents an integer of 0 or more
- R represents a hydrogen atom, an amino group, a hydroxyl group, or a monovalent or higher-valent organic group having one or more carbon atoms
- X represents any of halogen atoms
- Indicate the atom of the species, and Y and Z may be the same or different.
- R when ⁇ is 2 or more, R may be a divalent organic group bonded to two adjacent Y atoms.
- the aromatic nitro compound may have a condensed ring compound structure.
- R which is a monovalent or higher valent organic group, may have a structure in which the moiety bonded to Y ⁇ is represented by “—O—” or “—S—”.
- the reactant (aromatic halogen nitro compound) in the reaction system in which the reaction composition is used may have a structure represented by the following general formula (C2).
- n represents an integer of 1 or more
- m represents an integer of 1 or more
- ⁇ represents an integer of 0 or more
- ⁇ represents an integer of 0 or more
- R represents a hydrogen atom, an amino group, a hydroxyl group, or a monovalent or higher-valent organic group having one or more carbon atoms
- X represents any of halogen atoms
- Shows two atoms, Z represents an atom of C, N, O, or S when ⁇ 1, and at least selected from the group consisting of C, N, O, and S when ⁇ ⁇ 2.
- R which is a monovalent or higher valent organic group, may have a structure in which the moiety bonded to Y ⁇ is represented by “—O—” or “—S—”.
- the portion represented by “XJ-” is a structure represented by the following formulas (C2-1), (C2-2), (C2-3), and (C2-4) You may have.
- XC- (C O) -N- (C2-1)
- X ⁇ C C ⁇ C ⁇ (C2-2)
- X 1 and X 2 each represent one of halogen atoms, and X 1 and X 2 may be the same or different.
- the reaction composition may contain in advance an aromatic nitro compound as a reactant.
- an aromatic amine having at least one amino group obtained as a product by a hydrogenation reaction of an aromatic nitro compound may be further included.
- aromatic amine having one or more amino groups is desirably an aromatic halogenamine as a main product, but within the range where the effects of the present invention can be obtained (allowed in the reaction system used). There may be some aromatic amines that are dehalogenated (within range).
- the method for producing the reaction composition is not particularly limited, and a combination of known techniques can be employed.
- the catalyst contained in the reaction composition can be obtained, for example, by reducing a dispersion containing a Pt compound, an Fe compound, and water on a support to obtain a catalyst in which Pt particles and Fe oxide particles are supported on the support. Good.
- the support of Pt and the support of Fe oxide may be performed simultaneously as described above, or either one may be performed first and the other may be performed later.
- the order of mixing should take into account the respective chemical properties, and if they can be mixed well without causing undesired chemical reactions There is no particular limitation.
- the order of mixing is not particularly limited as long as they can be sufficiently mixed without causing an undesirable chemical reaction.
- the order of mixing is not particularly limited as long as the reactants can be sufficiently mixed with other components without causing undesired chemical reactions.
- the reaction composition of the present embodiment may be stored in a packaging body such as a container or a bag after production.
- the internal structure of the package that comes into contact with the reaction composition must be configured so as not to cause a chemical reaction with the reaction composition. By setting it as the state accommodated in the reaction composition package, the reaction composition can be easily moved from the production place to the use place when the production place and the use place of the reaction composition are different.
- the reaction system of this embodiment has the structure containing the reaction container which can accommodate the reaction composition of this invention as a reaction material.
- the reaction system of the present embodiment is not particularly limited as long as it has a configuration including a reaction vessel that can contain the reaction composition of the present invention as a reactant.
- the reaction system of the present embodiment is an aromatic nitro compound (aromatic halogen compound) having a structure in which one or more nitro groups and one or more halogen atoms are directly bonded as substituents in the same ring skeleton.
- aromatic nitro compound aromatic halogen compound
- the reaction system of the present embodiment may include the reaction composition of the present invention as a constituent element in advance.
- the reaction system may include the reaction composition of the present invention in advance in the reaction container, or may further include another container that can store and hold the reaction composition in advance in addition to the reaction container. In doing so, the reaction composition may be moved from the other container to the reaction container.
- reaction system of the present embodiment further includes another container that can previously store and hold the components of the reaction composition of the present invention, and before performing the hydrogenation reaction at the place where the hydrogenation reaction is performed.
- reaction composition may be supplied into a predetermined container to produce a reaction composition, and the produced reaction composition may be used for a hydrogenation reaction.
- the reaction system may be configured to have another container that can previously store and hold all of the components of the reaction composition of the present invention, or one of the components of the reaction composition of the present invention. It is good also as a structure which has another container which can accommodate and hold
- the reaction system may have a configuration further including another container that can previously store and hold the organic solvent, and the catalyst may be configured to be brought in from the manufacturing site of another catalyst.
- the reaction system of the present embodiment uses the reaction composition of the present invention, the nitro group of the aromatic nitro compound that is the reactant can be selectively hydrogenated, and the elimination of halogen atoms from the ring is sufficiently reduced. A hydrogenation reaction that can be performed can be realized.
- Example 1 As a catalyst, a catalyst in which Pt particles and Fe oxide particles are supported on a carbon support ⁇ trade name “NE-01M02”, Pt content 1.0 wt%, Fe content 0.20 wt%, N. E. CHEMCAT (hereinafter referred to as “Pt—FeOx / C” if necessary) ⁇ was prepared.
- the carbon support is activated carbon (specific surface area based on BET measurement is 900: m 2 / g), and the Fe oxide particles are mainly composed of Fe 2 O 3 (the result based on XPS analysis indicates Fe 2 O 3 is approximately 100%).
- Commercially available toluene was prepared as the organic solvent.
- Pt-FeOx / C powder 127.0 mg (water content 0.141 mL) and toluene 10 mL (organic solvent) were mixed to obtain a reaction composition.
- Example 2 The same Pt—FeOx / C catalyst powder 127.0 mg (water content 0.141 mL) as in Example 1 was dried (using a dryer, kept in air at 300 ° C. for 15 minutes), and a moisture meter The reaction composition of Example 2 was prepared using the same raw materials and preparation conditions as in Example 1 except that the water content measured in step 1 was adjusted to 0 mL.
- Example 3 A dehydrating agent was added to and mixed with 127.0 mg (water content 0.141 mL) of the same Pt—FeOx / C catalyst powder as in Example 1, and then 10 mL of toluene (organic solvent) was added to the reaction composition.
- a reaction composition of Example 3 was prepared using the same preparation conditions and the same raw materials as in Example 1 except that they were obtained.
- As a dehydrating agent 2 g of a zeolite (Molecular Sieves 4A) having a structure code “LTA” type which is commercially available was used.
- the amount of the dehydrating agent used is an amount capable of sufficiently dehydrating all of the water contained in the Pt—FeOx / C catalyst.
- Example 4 (Example 4) to (Example 9) Except that the value of ⁇ 100 ⁇ (Vh / Vs) ⁇ was changed to the value shown in Table 1, the same preparation conditions as in Example 1 and the same raw materials were used. A reaction composition was prepared.
- Comparative Example 1 A reaction composition of Comparative Example 1 was prepared using the same preparation conditions and the same raw materials as in Example 1 except that 1 mL of water was added to the same reaction composition as in Example 1.
- 2-bromo-5-nitropyridine represented by the formula (C1-1) has a heterocyclic structure having an N atom.
- 2-bromo-5-nitrobenzene having a structure in which the N atom in this heterocycle is replaced with a C atom 2-bromo-5-nitropyridine is a hydrogenation of the nitro group of the main reaction (main production)
- a side reaction debromination reaction (the by-product is 3-aminopyridine represented by the formula (C1-3)) It is a reaction product that proceeds easily.
- reaction product 2.5 mmol of 2-bromo-5-nitrobenzene represented by the formula (C1-1) Hydrogen pressure: 0.6 MPa Reaction temperature: 50 ° C. (Example 1, Example 2, Examples 4 to 9), 100 ° C. (Example 3, Comparative Example 1) Reaction time: 5 hours
- Tables 1 and 2 show the results obtained for the reaction compositions of Examples 1 to 9 and Comparative Examples 1 to 9.
- the reaction composition of the present example shows that the nitro group of the aromatic nitro compound having a structure in which the nitro group and the halogen atom are directly bonded to each other as a substituent in the same ring skeleton.
- the nitro group can be selectively hydrogenated and the elimination of halogen atoms from the ring can be sufficiently reduced.
- the reaction composition of the present invention comprises a nitro group of an aromatic nitro compound (aromatic halogen nitro compound) having a structure in which a nitro group and a halogen atom are directly bonded in the state of being separated into the same ring skeleton as a substituent.
- aromatic nitro compound aromatic halogen nitro compound
- the nitro group can be selectively hydrogenated, and it has a catalytic activity that can sufficiently reduce elimination of halogen atoms from the ring.
- the present invention contributes to the development of efficient mass production technology for aromatic halogenamines, which are important raw materials for pharmaceuticals, dyes, insecticides and herbicides. Contribute to development.
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Abstract
Description
すなわち、本発明は、
(N1)1以上のニトロ基と1以上のハロゲン原子とが置換基として同一の環の環骨格にそれぞれ分かれた状態で直接結合した構造を有する芳香族ニトロ化合物を反応物とし、前記1以上のニトロ基のうちの少なくとも1つをアミノ基に変換する水素化反応に用いられる触媒と、
溶媒と、
を含んでおり、
前記触媒は、担体と、前記担体上に担持されるPt粒子とFe酸化物粒子と、を含んでおり、
前記溶媒の構成成分が下記式(1)の条件を満たしている、
反応組成物。
0.00%≦{100×(Vh/Vs)}≦10.00%・・・(1)
[式(1)中、Vhは反応生成水以外に投入される水の体積(L)を示し、Vsは前記反応物の少なくとも一部を溶解可能な有機溶媒の体積(L)を示す。]
(N2)芳香族ニトロ化合物が更に含まれていてもよい。
(N3)芳香族ニトロ化合物の水素化反応により生成物として得られる少なくとも1つのアミノ基を有する芳香族アミンが更に含まれていてもよい。
(N4)溶媒の構成成分が下記式(2)の条件を更に満していることが更に好ましい。
1.00%≦{100×(Vh/Vs)}≦5.00%・・・(2)
(N5)脱水剤が更に含まれていてもよい。
本実施形態の反応組成物は、触媒と、溶媒とを含んでいる。
0.00%≦{100×(Vh/Vs)}≦10.00%・・・(1)
[式(1)中、Vhは反応生成水以外に投入される水の体積(L)を示し、Vsは前記反応物の少なくとも一部を溶解可能な有機溶媒の体積(L)を示す。]
1.00%≦{100×(Vh/Vs)}≦5.00%・・・(2)
脱水剤は、Pt粒子、Fe酸化物粒子と混合された状態において、常温、常圧でこれらと化学反応が進行しない安定性を有していれば特に制限されない。例えば、脱水剤としては、入手容易性などの観点から、ゼオライト、硫酸ナトリウム、硫酸マグネシウムが好ましく挙げられる。
nは、1以上の整数を示し、
mは、1以上の整数を示し、
αは、0以上の整数を示し、
βは、0以上の整数を示し、
5≦(n+m+α+β)≦6であり、
Rは、水素原子、アミノ基、水酸基、又は、炭素原子を1以上有する1価以上の有機基を示し、
Xは、ハロゲン原子のうちのいずれかを示し、
Yは、α=1の場合には、C、N、O、又は、Sの原子を示し、α≧2の場合は、C、N、O、及び、Sからなる群から選択される少なくとも2種の原子を示し、
Zは、β=1の場合には、C、N、O、又は、Sの原子を示し、β≧2の場合は、C、N、O、及び、Sからなる群から選択される少なくとも2種の原子を示し、かつ、
YとZとは同一であっても異なっていてもよい。
nは、1以上の整数を示し、
mは、1以上の整数を示し、
αは、0以上の整数を示し、
βは、0以上の整数を示し、
5≦(n+m+α+β)≦6であり、
Rは、水素原子、アミノ基、水酸基、又は、炭素原子を1以上有する1価以上の有機基を示し、
Xは、ハロゲン原子のうちのいずれかを示し、
Yは、α=1の場合には、C、N、O、又は、Sの原子を示し、α≧2の場合には、C、N、O、及び、Sからなる群から選択される少なくとも2種の原子を示し、
Zは、β=1の場合には、C、N、O、又は、Sの原子を示し、β≧2の場合には、C、N、O、及び、Sからなる群から選択される少なくとも2種の原子を示し、
YとZとは同一であっても異なっていてもよく、
Jは炭素原子を1以上有する2価の有機基を示し、m≧2の場合には、Jは同一であっても異なっていてもよい。
X-C-(C=O)-N- ・・・(C2-1)
X-C=C-C- ・・・(C2-2)
X-C-C- ・・・(C2-3)
また、この場合、芳香族ニトロ化合物の水素化反応により生成物として得られる少なくとも1つのアミノ基を有する芳香族アミンが更に含まれていてもよい。
反応組成物の製造方法は、特に限定されず公知の手法の組合せを採用できる。
本実施形態の反応システムは、本発明の反応組成物を反応物として収容可能な反応容器を含む構成を有している。
(実施例1)
触媒として、カーボン担体に、Pt粒子と、Fe酸化物粒子とが担持された触媒{商品名「NE-01M02」、Ptの含有量1.0wt%、Feの含有量0.20wt%、N.E.CHEMCAT社製(以下、必要に応じて「Pt-FeOx/C」と表記)}を用意した。
このPt-FeOx/Cは、カーボン担体が活性炭(BET測定に基づく比表面積が900:m2/g)であり、Fe酸化物粒子は主成分がFe2O3(XPS分析に基づく結果ではFe2O3が略100%)のものである。
有機溶媒として市販のトルエンを用意した。
Pt-FeOx/Cの粉体127.0mg(含水量0.141mL)と、トルエン10mL(有機溶媒)を混合し、反応組成物を得た。
実施例1と同一のPt-FeOx/C触媒の粉体127.0mg(含水量0.141mL)を乾燥処理(乾燥機を使用し、空気中、300℃、15分間保持)し、水分率計で計測される含水量を0mLに調製したものを使用したこと以外は、実施例1と同様の調製条件、同一の原料を使用して、実施例2の反応組成物を調製した。
実施例1と同一のPt-FeOx/C触媒の粉体127.0mg(含水量0.141mL)に脱水剤を添加し混合し、その後、トルエン10mL(有機溶媒)を混合し、反応組成物を得たこと以外は実施例1と同様の調製条件、同一の原料を使用して、実施例3の反応組成物を調製した。
脱水剤は、市販されている構造コード「LTA」型のゼオライト(Molecular Sieves 4A)を2g使用した。脱水剤の使用量はPt-FeOx/C触媒に含まれる水分の全てを十分に脱水可能な量である。
{100×(Vh/Vs)}の値を表1に示した値に変更したこと以外は、実施例1と同様の調製条件、同一の原料を使用して、実施例4~実施例9の反応組成物を調製した。
実施例1と同一の反応組成物に対し、水を1mL添加したこと以外は実施例1と同様の調製条件、同一の原料を使用して、比較例1の反応組成物を調製した。
反応物:式(C1-1)で示される2-ブロモ-5-ニトロベンゼン 2.5mmol
水素圧 :0.6MPa
反応温度:50℃(実施例1、実施例2、実施例4~実施例9)、100℃(実施例3、比較例1)
反応時間:5時間
Claims (6)
- 1以上のニトロ基と1以上のハロゲン原子とが置換基として同一の環の環骨格にそれぞれ分かれた状態で直接結合した構造を有する芳香族ニトロ化合物を反応物とし、前記1以上のニトロ基のうちの少なくとも1つをアミノ基に変換する水素化反応に用いられる触媒と、
溶媒と、
を含んでおり、
前記触媒は、担体と、前記担体上に担持されるPt粒子とFe酸化物粒子と、を含んでおり、
前記溶媒の構成成分が下記式(1)の条件を満たしている、
反応組成物。
0.00%≦{100×(Vh/Vs)}≦10.00%・・・(1)
[式(1)中、Vhは反応生成水以外に投入される水の体積(L)を示し、Vsは前記反応物の少なくとも一部を溶解可能な有機溶媒の体積(L)を示す。] - 前記芳香族ニトロ化合物が更に含まれている、
請求項1に記載の反応組成物。 - 前記芳香族ニトロ化合物の前記水素化反応により生成物として得られる少なくとも1つのアミノ基を有する芳香族アミンが更に含まれている
請求項2に記載の反応組成物。 - 前記溶媒の構成成分が下記式(2)の条件を更に満している、
請求項1~3のうちのいずれか1項に記載の反応組成物。
1.00%≦{100×(Vh/Vs)}≦5.00%・・・(2) - 脱水剤が更に含まれている、
請求項1~4のうちのいずれか1項に記載の反応組成物。 - 請求項1~5のうちのいずれか1項に記載の反応組成物を反応物として収容可能な反応容器を含む、反応システム。
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CN201780019207.5A CN109070063A (zh) | 2016-03-23 | 2017-02-15 | 反应组合物和使用该反应组合物的反应体系 |
JP2018507130A JPWO2017163681A1 (ja) | 2016-03-23 | 2017-02-15 | 反応組成物及びこれを用いた反応システム |
EP17769728.1A EP3434367A4 (en) | 2016-03-23 | 2017-02-15 | REACTION COMPOSITION AND REACTION SYSTEM USING THEREOF |
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Citations (3)
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US5068436A (en) * | 1989-03-10 | 1991-11-26 | E. I. Du Pont De Nemours And Company | Hydrogenation of halonitrobenzenes without dehalogenation |
JPH0671178A (ja) * | 1992-06-09 | 1994-03-15 | Degussa Ag | ハロゲンニトロ芳香族化合物の選択的水素化のための担体付変性貴金属触媒およびその製造方法 |
JP2000302738A (ja) * | 1999-04-16 | 2000-10-31 | Wakayama Seika Kogyo Kk | 2−トリフルオロメチル−4,4’−ジアミノジフェニルエーテルおよびその製造方法 |
Family Cites Families (2)
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US4212824A (en) * | 1978-07-11 | 1980-07-15 | E. I. Du Pont De Nemours And Company | Hydrogenation catalyst with improved metallic distribution, its preparation and use for the reduction of aromatic nitro compounds |
US4990663A (en) * | 1989-05-15 | 1991-02-05 | E. I. Du Pont De Nemours And Company | Process for preparing halogenated aromatic amines |
-
2017
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- 2017-02-15 EP EP17769728.1A patent/EP3434367A4/en not_active Withdrawn
- 2017-02-15 CN CN201780019207.5A patent/CN109070063A/zh active Pending
- 2017-02-15 JP JP2018507130A patent/JPWO2017163681A1/ja not_active Withdrawn
- 2017-02-15 WO PCT/JP2017/005584 patent/WO2017163681A1/ja active Application Filing
Patent Citations (3)
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US5068436A (en) * | 1989-03-10 | 1991-11-26 | E. I. Du Pont De Nemours And Company | Hydrogenation of halonitrobenzenes without dehalogenation |
JPH0671178A (ja) * | 1992-06-09 | 1994-03-15 | Degussa Ag | ハロゲンニトロ芳香族化合物の選択的水素化のための担体付変性貴金属触媒およびその製造方法 |
JP2000302738A (ja) * | 1999-04-16 | 2000-10-31 | Wakayama Seika Kogyo Kk | 2−トリフルオロメチル−4,4’−ジアミノジフェニルエーテルおよびその製造方法 |
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HAN, XIAOXIANG ET AL.: "Influence of support and transition metal (Cr, Mn, Fe, Co, Ni and Cu)on the hydrogenation of p-chloronitrobenzene over supported platinum catalysts", CATALYSIS TODAY, vol. 93-95, 8 July 2004 (2004-07-08), pages 433 - 437, XP027186054, ISSN: 0920-5861 * |
See also references of EP3434367A4 * |
WANG, XIANGDONG ET AL.: "Enhanced Catalytic Hydrogenation Activity and Selectivity of Pt- MxOy/Al2O3 (M = Ni, Fe, Co) Heteroaggregate Catalysts by in Situ Transformation of PtM Alloy Nanoparticles", THE JOURNAL OF PHYSICAL CHEMISTRY C, vol. 117, 20 March 2013 (2013-03-20), pages 7294 - 7302, XP055425092, ISSN: 1932-7455 * |
XU, XIANGSHENG ET AL.: "A highly active and chemoselective assembled Pt/C(Fe) catalyst for hydrogenation of o-chloronitrobenzene", APPLIED CATALYSIS A : GENERAL, vol. 429-430, 4 April 2012 (2012-04-04), pages 17 - 23, XP028489224, ISSN: 0926-860X * |
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US20200290967A1 (en) | 2020-09-17 |
JPWO2017163681A1 (ja) | 2019-01-31 |
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