Patent Application
20170204049
The present invention relates to a method for producing bis(aminomethyl)cyclohexane.
Bis(aminomethyl)cyclohexane is an industrially important compound to be used as a raw material for e.g., epoxy hardeners, polyamides and polyurethanes. A bis(aminomethyl)cyclohexane has two isomers, i.e., a cis-isomer and a trans-isomer, derived from the cyclohexane ring. It is known that the physical properties of a polymer obtained by using a bis(aminomethyl)cyclohexane greatly vary depending upon the ratio of isomers, i.e., ratio of a cis-isomer and a trans-isomer.
For example, in a polyamide obtained by using 1,4-bis(aminomethyl)cyclohexane, it is known that, as the content of a trans-isomer increases, the melting point of the polyamide increases, with the result that the polyamide becomes highly heat resistant (Non Patent Literature 1). It is also known that a polyurethane obtained by using 1,4-bisisocyanatomethyl cyclohexane derived from 1,4-bis(aminomethyl)cyclohexane is improved in physical properties required for various applications as the content of the trans-isomer increases (Patent Literature 1).
It is further shown that, in a polyamide obtained by using 1,3-bis(aminomethyl)cyclohexane, a polyamide having a high cis-isomer content has a high crystallinity; whereas a polyamide having a high trans-isomer content is amorphous (Non Patent Literature 2).
For these reasons, it is extremely important to control the isomer ratio of a bis(aminomethyl)cyclohexane.
A bis(aminomethyl)cyclohexane is produced by a technique known in the art. More specifically, a bis(aminomethyl)cyclohexane is obtained by hydrogenating an aromatic dinitrile in the presence of a catalyst to synthesize a xylylenediamine and nuclear-hydrogenating the xylylenediamine in the presence of a catalyst.
Many methods are known for producing a xylylenediamine by hydrogenating an aromatic dinitrile. For example, a method of using a Raney catalyst such as a Raney nickel and a Raney cobalt, is disclosed (Patent Literature 3).
Many methods are reported for producing a bis(aminomethyl)cyclohexane by nuclear-hydrogenating a xylylenediamine. For example, a method of using a catalyst such as ruthenium immobilized on a carrier is disclosed (Patent Literature 4)
In the nuclear hydrogenation reaction of a xylylenediamine, a cis-isomer is more easily produced than a trans-isomer, in other words, it is difficult to selectively synthesize a trans-isomer. The ratio of a bis(aminomethyl)cyclohexane trans-isomer produced by this method is generally 50% or less. Because of this, to obtain a 1,4-bis(aminomethyl)cyclohexane having a high trans-isomer content, an isomerization reaction is proposed.
For example, a method for obtaining trans-1,4-bis(aminomethyl)cyclohexane by isomerizing a 1,4-bis(aminomethyl)cyclohexane in the presence of a noble metal catalyst such as platinum and ruthenium is disclosed (Patent Literatures 4 to 6). However, since a content of a trans-isomer produced in one path (single step) remains at about 80%. In order to obtain a trans-isomer in a high-concentration, separation by distillation and crystallization, and recycling are required, in short, a complicated process is required. In this method, isomerization must be carried out in liquid ammonia to obtain 1,4-bis(aminomethyl)cyclohexane in a high recovery rate. Accordingly, this method has a drawback in handling liquid ammonia and being a high-pressure reaction. Nevertheless, if liquid ammonia is not used, the recovery rate of 1,4-bis(aminomethyl)cyclohexane decreases.
In the meantime, a method for isomerizing 1,4-bis(aminomethyl)cyclohexane by mixing 1,4-bis(aminomethyl)cyclohexane with a benzylamine compound and an alkali metal, an alkali metal hydride or an alkali metal amide is disclosed (Patent Literature 7). However, it is shown that the final isomer ratio, i.e., a trans/cis ratio, is 4.0 (trans-isomer ratio: about 80%) and isomerization does not proceed any more in this method.
These isomerization reactions have a limitation in that a cis-isomer and a trans-isomer reach an equilibrium state. Thus, it is not easy to obtain 1,4-bis(aminomethyl)cyclohexane containing a trans-isomer more than an equilibrium composition.
In another method (Patent Literature 8) known in the art, trans-1,4-bis(aminomethyl)cyclohexane is obtained by derivatizing 1,4-bis(aminomethyl)cyclohexane to an aldimine compound, and isomerizing and decomposing the aldimine compound.
Also, a method for obtaining a 1,4-bis(aminomethyl)cyclohexane having a high trans-isomer content using terephthalic acid as a raw material via cyclohexane dicarboxylic acid is disclosed (Patent Literature 9). This method discloses that, to increase the content of a trans-isomer, a precursor, 1,4-dicyanocyclohexane, is crystallized to separate a trans-isomer and the remaining cis-isomer is isomerized and recycled.
In the method described in Patent Literature 8, a trans-isomer is obtained in an extremely high ratio of 99%; however, three steps are required for isomerization; an aldehyde, from which a derivative is obtained, must be recycled through very complicated step. For these reasons, it is not easy to industrially carry out this method.
In the method described in Patent Literature 9, an extremely long step is required and industrially unfavorable.
In the prior art, an industrial technical process for producing 1,4-bis(aminomethyl)cyclohexane having an equilibrium composition (a trans-isomer ratio: 83% or more) in a single step has not yet been established. More specifically, in order to produce a 1,4-bis(aminomethyl)cyclohexane having an equilibrium composition or more (trans-isomer ratio: 83% or more), a step of returning 1,4-bis(aminomethyl)cyclohexane having an equilibrium composition or less (trans-isomer ratio: 83% or less) again to an isomerization step is required, with the result that two steps or more are required.
The present invention was attained in consideration of the aforementioned problems. An object of the present invention is to provide a method for producing a bis(aminomethyl)cyclohexane having a content of an isomer beyond that for an equilibrium composition in a simple process suitable for industrialization.
The present inventors intensively conducted studies to solve the aforementioned problems. As a result, they found that the above problems can be solved by a production method of carrying out an isomerization step and a distillation step at the same time, and arrived at the present invention.
More specifically, the present invention is as follows.
[1]
A method for producing a bis(aminomethyl)cyclohexane comprising:
an isomerization step of isomerizing a cis-isomer of 1,4-bis(aminomethyl)cyclohexane and/or a trans-isomer of 1,3-bis(aminomethyl)cyclohexane at a bottom part of a distillation tower to obtain a trans-isomer of 1,4-bis(aminomethyl)cyclohexane and/or a cis-isomer of 1,3-bis(aminomethyl)cyclohexane; and
a distillation step of separating the trans-isomer of 1,4-bis(aminomethyl)cyclohexane and/or the cis-isomer of 1,3-bis(aminomethyl)cyclohexane by distillation, in a top part of the distillation tower, wherein
an isomerization reaction temperature of the isomerization step is 80 to 140° C.; and
the isomerization step and the distillation step are simultaneously carried out.
[2]
The method for producing the bis(aminomethyl)cyclohexane according to the above [1], wherein a content of the trans-isomer in the 1,4-bis(aminomethyl)cyclohexane obtained from the top part of the tower in the distillation step is 84% or more.
[3]
The method for producing the bis(aminomethyl)cyclohexane according to the above [1] or [2], wherein the content of the trans-isomer in the 1,4-bis(aminomethyl)cyclohexane obtained from the top part of the tower in the distillation step is 90% or more.
[4]
The method for producing the bis(aminomethyl)cyclohexane according to any one of the above [1] to [3], wherein, in the isomerization step, the cis-isomer of 1,4-bis(aminomethyl)cyclohexane and/or the trans-isomer of 1,3-bis(aminomethyl)cyclohexane are isomerized in the presence of
at least one compound selected from the group consisting of an alkali metal, an alkali metal-containing compound, an alkaline-earth metal and an alkaline-earth metal-containing compound, and
a benzylamine compound.
[5]
The method for producing the bis(aminomethyl)cyclohexane according to the above [4], wherein the benzylamine compound is at least one selected from the group consisting of benzylamine, 3-methylbenzylamine, 4-methylbenzylamine, dibenzylamine, metaxylylenediamine and paraxylylenediamine.
[6]
The method for producing the bis(aminomethyl)cyclohexane according to the above [4] or [5], wherein the alkali metal comprises metallic sodium.
[7]
The method for producing the bis(aminomethyl)cyclohexane according to any one of the above [1] to [6], wherein the alkali metal-containing compound comprises at least one selected from the group consisting of an alkali metal hydride and an alkali metal amide.
[8]
The method for producing the bis(aminomethyl)cyclohexane according to the above [7], wherein the alkali metal hydride comprises sodium hydride.
[9]
The method for producing the bis(aminomethyl)cyclohexane according to the above [7], wherein the alkali metal amide comprises sodium amide.
[10]
A 1,4-bis(aminomethyl)cyclohexane comprising a trans-isomer content of 84% or more and obtained by the method for producing the bis(aminomethyl)cyclohexane according to any one of the above [1] to [9].
According to this invention, it is possible to provide a method for producing a bis(aminomethyl)cyclohexane having an isomer content beyond an equilibrium composition in a simple process suitable for industrialization.
Now, embodiments (hereinafter referred to as “the present embodiment”) for carrying out the invention will be more specifically described below; however, the present invention is not limited to these and can be modified without departing from the scope of the invention.
The method for producing a bis(aminomethyl)cyclohexane according to the present embodiment has
an isomerization step of isomerizing a cis-isomer of 1,4-bis(aminomethyl)cyclohexane and/or a trans-isomer of 1,3-bis(aminomethyl)cyclohexane at the bottom part of a distillation tower to obtain a trans-isomer of 1,4-bis(aminomethyl)cyclohexane and/or a cis-isomer of 1,3-bis(aminomethyl)cyclohexane; and
a distillation step of separating the trans-isomer of 1,4-bis(aminomethyl)cyclohexane and/or the cis-isomer of 1,3-bis(aminomethyl)cyclohexane by distillation, in the top of the distillation tower, in which
the isomerization reaction temperature in the isomerization step is 80 to 140° C., and
the isomerization step and the distillation step are simultaneously carried out.
In the method for producing a bis(aminomethyl)cyclohexane according to the present embodiment, if the isomerization step and the distillation step are simultaneously carried out, a 1,4-bis(aminomethyl)cyclohexane having a content of a trans-isomer exceeding that for an equilibrium composition or 1,3-bis(aminomethyl)cyclohexane having a content of a cis-isomer exceeding that for an equilibrium composition can be produced in a simple process.
The term “simultaneous” used herein means not only the case where the initiation and termination points of the isomerization step completely coincide with those of the distillation step but also the case where the isomerization step and the distillation step are partially overlapped; more specifically, refers to the case where a bis(aminomethyl)cyclohexane is separated while isomerizing.
More specifically, if the production method of the present embodiment is carried out in a batch system, the following method may be mentioned: raw materials are supplied to the bottom part of a distillation tower and an isomerization reaction was carried out at the bottom part of the tower; at the same time, a desired isomer is separated by distillation and obtained from the top part of the distillation tower. In contrast, if the production method of the present embodiment is carried out in a continuous system, the following method may be mentioned: raw materials are continuously supplied to the bottom part of a distillation tower and an isomerization reaction is carried out at the bottom part of the tower; at the same time, a desired isomer is continuously separated by distillation and obtained from the top part of the distillation tower. Among them, the continuous system is preferable in view of industrialization.
A schematic view of an apparatus for producing a bis(aminomethyl)cyclohexane according to the present embodiment is shown in
The distillation tower is not particularly limited as long as a cis-isomer and a trans-isomer can be separated and may have a structure known in the art. For example, a packed tower charged with regular packing or irregular packing and a tray tower having trays can be used. Among them, a packed tower charged with regular packing, in which differential pressure is most unlikely produced, is preferably used in order to prevent a temperature increase during an isomerization reaction. The distillation tower may have e.g., a heater for heating a mixture of a cis-isomer and a trans-isomer of a bis(aminomethyl)cyclohexane present at the bottom part, a stirrer for stirring the mixture and a pressure control mechanism for controlling reaction pressure.
The isomerization step is a step of isomerizing a cis-isomer of 1,4-bis(aminomethyl)cyclohexane and/or a trans-isomer of 1,3-bis(aminomethyl)cyclohexane at the bottom part of a distillation tower to obtain a trans-isomer of 1,4-bis(aminomethyl)cyclohexane and/or a cis-isomer of 1,3-bis(aminomethyl)cyclohexane.
The term “isomerize” refers to converting a trans-isomer of 1,3-bis(aminomethyl)cyclohexane to a cis-isomer thereof or a cis-isomer of 1,4-bis(aminomethyl)cyclohexane to a trans-isomer thereof.
In the production method of the present embodiment, for example, in the isomerization step, a mixture of a cis-isomer and a trans-isomer of 1,4-bis(aminomethyl)cyclohexane is subjected to an isomerization reaction to isomerize the cis-isomer of 1,4-bis(aminomethyl)cyclohexane to a trans-isomer of 1,4-bis(aminomethyl)cyclohexane; and a mixture of a cis-isomer and a trans-isomer of 1,3-bis(aminomethyl)cyclohexane is subjected to an isomerization reaction to isomerize the trans-isomer of 1,3-bis(aminomethyl)cyclohexane to a cis-isomer of 1,3-bis(aminomethyl)cyclohexane.
In the isomerization step, the isomerization reaction temperature (tower-bottom temperature) is 80 to 140° C. and preferably 100 to 140° C. If the isomerization reaction temperature is 80° C. or more, the isomerization reaction can be more efficiently carried out. In contrast, if the isomerization reaction temperature is 140° C. or less, a side reaction such as a decomposition reaction of a bis(aminomethyl)cyclohexane can be suppressed, production of side products such as low-boiling products and high-boiling products can be reduced. As a result, a desired isomer of a bis(aminomethyl)cyclohexane can be easily and continuously distilled to improve a yield thereof.
The isomerization reaction can be carried out either in the presence or absence of a solvent. As the solvent that can be used, although it is not particularly limited, for example, an inert solvent is mentioned. Examples of such a solvent include, but are not particularly limited to, aromatic solvents such as benzene, toluene or xylene; ether solvents such as diethyl ether or tetrahydrofuran; and hydrocarbon solvents such as hexane or heptane.
As the isomerization reaction atmosphere, although it is not particularly limited, for example, an atmosphere not containing air or active hydrogen such as water or an alcohol, is preferable. If such an atmosphere is employed, the reaction efficiency tends to be more improved. Particularly, in view of the reaction efficiency, the water content in the reaction system is preferably controlled to be 1000 ppm or less. As a simple method for reducing the content of water in a reaction system, an isomerization reaction is preferably carried out in an atmosphere of an inert gas such as nitrogen gas and argon gas.
In the method for producing a bis(aminomethyl)cyclohexane according to the present embodiment, 1,3-bis(aminomethyl)cyclohexane and/or 1,4-bis(aminomethyl)cyclohexane are used. Among them, in view of the effect of the present invention, 1,4-bis(aminomethyl)cyclohexane is preferable. Note that 1,3-bis(aminomethyl)cyclohexane and 1,4-bis(aminomethyl)cyclohexane each may be a mixture of a trans-isomer and a cis-isomer.
As a method for producing a cis-isomer and a trans-isomer of a bis(aminomethyl)cyclohexane or a mixture thereof used in this embodiment, although it is not limited, for example, a method of nuclear-hydrogenating para-xylylenediamine or terephthalonitrile in the presence of a noble metal catalyst such as ruthenium, palladium, rhodium and platinum, is mentioned. The trans-isomer herein is obtained in a ratio of 50% or less and the resultant bis(aminomethyl)cyclohexane or mixture can be used without particularly changing an isomer ratio.
In the isomerization step, a cis-isomer of the 1,4-bis(aminomethyl)cyclohexane and/or a trans-isomer of 1,3-bis(aminomethyl)cyclohexane are preferably isomerized in the presence of at least one compound selected from the group consisting of an alkali metal, an alkali metal-containing compound, an alkaline earth metal and an alkaline earth metal-containing compound (hereinafter collectively referred to as an “alkali metal(s)”) and a benzylamine compound. Owing to this, the rate of isomerization is further improved and a recovery rate tends to be more improved.
Example of the benzylamine compound include, but are not limited to, for example, monobenzylamine compounds such as benzylamine, 2-methylbenzylamine, 3-methylbenzylamine, 4-methylbenzylamine; secondary benzylamine compounds such as dibenzylamine and N-methylbenzylamine; and compounds having two aminomethyl groups such as metaxylylenediamine and paraxylylenediamine. Among them, in view of reaction efficiency, at least one selected from the group consisting of benzylamine, 3-methylbenzylamine, 4-methylbenzylamine, dibenzylamine, metaxylylenediamine and paraxylylenediamine, is preferable. These compounds may be used alone or in combination of two or more.
The use amount of benzylamine compound relative to bis(aminomethyl)cyclohexane (100 wt %) is preferably 0.10 to 10 wt % and more preferably 0.50 to 4.0 wt %. If the use amount of benzylamine compound falls within the above range, an isomerization reaction tends to more efficiently proceed.
The compound that can be used in the isomerization step is at least one compound selected from the group consisting of an alkali metal, an alkali metal-containing compound, an alkaline-earth metal, and an alkaline-earth metal containing compound. If such a compound is used, an isomerization reaction can more efficiently proceed. These compounds may be used alone or in combination of two or more.
Among them, at least one compound selected from the group consisting of a metallic sodium, a sodium amide and a sodium hydride is preferably included. If such a compound is used, the ratio of a trans-isomer or a cis-isomer in the resultant isomers and the isomerization yield tend to be improved.
Examples of the alkali metals include, but are not particularly limited to, a metallic sodium, a metallic potassium and a metallic lithium.
Examples of the alkali metal-containing compounds include, but are not particularly limited to, an alkali metal hydride, an alkali metal amide and a basic oxide. If such a compound is used, the ratio of a trans-isomer or a cis-isomer in the resultant isomers and the isomerization yield tend to be improved. Among them, at least one selected from the group consisting of an alkali metal hydride and an alkali metal amide, is preferable. Examples of the alkali metal hydride herein include, but are not particularly limited to, sodium hydride, potassium hydride, lithium hydride, lithium aluminum hydride and sodium boron hydride. Examples of the alkali metal amide include, but are not particularly limited to, sodium amide, potassium amide, lithium amide, lithium diisopropylamide and sodium bis(trimethylsilyl)amide. Examples of the basic oxide include, but are not particularly limited to, lithium oxide, sodium oxide, potassium oxide, cesium oxide, magnesium oxide, calcium oxide, strontium oxide and barium oxide.
Examples of the alkaline-earth metal include, but are not particularly limited to, metallic magnesium and metallic calcium.
Examples of the alkaline-earth metal-containing compound include, but are not particularly limited to, an alkaline earth metal hydride. Examples of the alkaline earth metal hydride include, but are not particularly limited to, calcium hydride and magnesium hydride.
The use amount of alkali metal or the like relative to one equivalent of a benzylamine compound is preferably 0.10 to 10 molar equivalent and more preferably 1 to 4 molar equivalent. If the use amount of alkali metal or the like falls within the above range, an isomerization reaction tends to more successfully and efficiently proceed.
The distillation step is a step of separating a trans-isomer of 1,4-bis(aminomethyl)cyclohexane and/or a cis-isomer of 1,3-bis(aminomethyl)cyclohexane by distillation, in the top part of the distillation tower. In the distillation step, not only a trans-isomer of 1,4-bis(aminomethyl)cyclohexane and/or a cis-isomer of 1,3-bis(aminomethyl)cyclohexane obtained by the above isomerization step but also a trans-isomer of 1,4-bis(aminomethyl)cyclohexane and/or a cis-isomer of 1,3-bis(aminomethyl)cyclohexane present in raw materials in the above isomerization step can be distilled.
In the distillation step, the content of a trans-isomer in 1,4-bis(aminomethyl)cyclohexane obtained from the tower top part is preferably 84% or more and more preferably 90% or more. Note that the term “%” used herein refers to mol %.
Isomerization must be carried out at a tower-bottom temperature within the range of 80 to 140° C. and more preferably 100 to 140° C. If the isomerization reaction temperature is 80° C. or more, the isomerization reaction tends to proceed more efficiently. In contrast, if the tower-bottom temperature exceeds 140° C., the boiling point increases and the recovery rate of distillation decreases.
Now, the present invention will be more specifically described by way of Examples and Comparative Examples; however, the present invention is not limited to these Examples.
Isomer compositions (cis/trans ratio) were analyzed by a gas chromatographic apparatus equipped with a capillary column, CP-Volamine manufactured by Valian. The trans-isomer of 1,4-bis(aminomethyl)cyclohexane has a lower boiling point than the cis-isomer thereof. The isomer first detected by gas chromatography was the trans-isomer and the cis-isomer was detected thereafter. The cis-isomer of 1,3-bis(aminomethyl)cyclohexane has a lower boiling point than the trans-isomer thereof. The isomer first detected by gas chromatography is the cis-isomer and the trans-isomer was detected thereafter. The ratio of the trans-isomer was calculated in accordance with the expression:
Area value of trans-isomer/(area value for cis-isomer+area value for trans-isomer)×100.
The ratio of the cis-isomer was calculated by the ratio to the trans-isomer from 100.
Recovery rates were obtained by calculating the weight of a bis(aminomethyl)cyclohexane in accordance with the internal standard method of the above gas chromatography analysis, and then, in accordance with the following expression.
Recovery rate (%)=(bis(aminomethyl)cyclohexane in distillate+bis(aminomethyl)cyclohexane held in packed tower+bis(aminomethyl)cyclohexane in bottom part)/(starting bis(aminomethyl)cyclohexane)×100
The distillation rate was calculated in accordance with the following expression.
Distillation rate (%)=bis(aminomethyl)cyclohexane in distillate/starting bis(aminomethyl)cyclohexane×100
1,4-Bis(aminomethyl)cyclohexane having an isomer composition (cis/trance ratio) of 59.3/40.7 used herein was obtained by nuclear-hydrogenation of paraxylylenediamine in the presence of a catalyst of Ru-alumina and in accordance with a known technique (for example, Patent Literature 2) and purified by distillation.
As the distillation tower, the tower shown in
To 1,4-bis(aminomethyl)cyclohexane (6 g) having an isomer composition (cis/trance ratio) of 59.3/40.7, 4-methylbenzylamine (4-MBA)(0.2 g) and sodium amide (0.2 g) were added. The isomerization reaction was carried out under an argon atmosphere at 120° C. and for 4 hours. Note that distillation was not carried out. The isomer composition after the isomerization (cis/trance ratio) was 17/83 and the recovery rate was 96.3%. The isomerization reaction was continued for further two hours; however, the isomer ratio did not change. From this, it is consider that the isomer composition reached an equilibrium.
1,4-Bis(aminomethyl)cyclohexane (107 g) having an isomer composition (cis/trance ratio) of 59.3/40.7 was weighed and placed in a distillation tower (theoretical stages: 7) packed with Sulzer pack having an inner diameter of 25 mm, and distillated in the following conditions. The maximum ratio of the trans-isomer of 1,4-bis(aminomethyl)cyclohexane obtained was 67.5%. The trans-isomer ratio decreased as the distillation rate increased. The trans-isomer ratio changed with the distillation rate is shown in
Tower-bottom temperature: 104 to 113° C.
Tower-top pressure: 2.3 to 4.5 mmHg
Tower-bottom pressure: 3.5 to 5.3 mmHg
Reflux ratio: 60 to 120
In the bottom part of a distillation tower (theoretical stages: 7) packed with Sulzer pack having an inner diameter of 25 mm, 1,4-bis(aminomethyl)cyclohexane (201 g) having an isomer composition (cis/trance ratio) of 59.3/40.7, 4.2 g of 4-methylbenzylamine (4-MBA) and sodium amide (1.6 g) were placed. Ten hours later, distillation and isomerization reaction were performed in the following conditions.
Tower-bottom temperature: 104 to 113° C.
Tower-top pressure: 2.3 to 4.5 mmHg
Tower-bottom pressure: 3.5 to 5.3 mmHg
Reflux ratio: 60 to 120
Even if the distillation rate increased, the ratio of a trans-isomer did not decrease and 90% or more of 1,4-bis(aminomethyl)cyclohexane was stably obtained. In total, 89% of the distillate was recovered and an average isomer composition (cis/trance ratio) was 8/92. Furthermore, the recovery rate of 1,4-bis(aminomethyl)cyclohexane including that in the bottom liquid was 93% and the isomer composition (cis/trance ratio) was 9/91. If the method of the invention is used, it is possible to obtain 1,4-bis(aminomethyl)cyclohexane having a trans-isomer ratio exceeding the equilibrium composition (isomer composition (cis/trance ratio):17/83). 1,4-Bis(aminomethyl)cyclohexane was obtained in a high recovery rate. The trans-isomer ratio changed with the distillation rate is shown in
The isomerization reaction and distillation were carried out in the same manner as in Example 1 except that 1,4-bis(aminomethyl)cyclohexane (150 g) having an isomer composition (cis/trance ratio) of 59.3/40.7, 6.2 g of 4-methylbenzylamine (4-MBA) and sodium amide (6.2 g) were used. In total, 70% of distillate was recovered. The average isomer composition (cis/trance ratio) was 7.1/92.9. The recovery rate of 1,4-bis(aminomethyl)cyclohexane including that in the bottom liquid was 90.6% and the isomer composition (cis/trance ratio) was 9.2/90.8. The trans-isomer ratio changed with the distillation rate is shown in
To 1,4-bis(aminomethyl)cyclohexane (200 g) having an isomer composition (cis/trance ratio) of 59.3/40.7, 8 g of 4-methylbenzylamine (4-MBA) and sodium amide (8 g) were added, and an isomerization reaction was carried out under an argon atmosphere at 120° C. for 5 hours.
After the isomerization reaction, the reaction solution was placed in the bottom of Oldershaw (theoretical stages: 20) distillation tower. While an isomerization reaction was carried out at the bottom part of the distillation tower, distillation was carried out in the following conditions. When the distillation rate exceeded 28%, abnormal bubbling of the tower-bottom liquid and an increase of viscosity occurred, which made it difficult to continue distillation. As a result of analysis of the tower-bottom liquid, high-boiling components produced was 60% or more. The recovery rate of 1,4-bis(aminomethyl)cyclohexane including that in the bottom liquid was up to 42%.
Tower-bottom temperature: 150 to 165° C.
Tower-top pressure: 15 mmHg
Tower-bottom pressure: 37 to 39 mmHg
Reflux ratio: 120
The present application was made based on Japanese Patent Application No. 2013-191881 filed on Sep. 17, 2013 with Japan Patent Office, the contents of which are incorporated herein by reference.
The present invention has industrial applicability as a method for producing a bis(aminomethyl)cyclohexane effective as an optical material using a polyamide and a polyurethane, such as plastic lenses, prisms, optical fibers, information recording substrates and filters.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2013-191881 | Sep 2013 | JP | national |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 15021841 | Mar 2016 | US |
| Child | 15477470 | US |
