KR20110011917A - Process for preparing of n-methyl pyrrolidone - Google Patents

Abstract

PURPOSE: A method for preparing N-methyl prolidone is provided to save energy and easily isolating N-methyl pyrolidone. CONSTITUTION: A method for preparing N-methyl prolidone comprises: a step of supplying monomethylamine(MMA) solution and gamma-butyrolactone(GBL) into a reactor; a step of separating N-methyl pyrolidone(NMP) and water; a step of mixing the water and monomethylamine to prepare monomethylamine solution; and a step of introducing the solution into a reactor. The monomethyl amine solution contains 25-65 weight% of monomethylamine and 35-75 weight% of water.

Description

Production method of N-methyl pyrrolidone {PROCESS FOR PREPARING OF N-METHYL PYRROLIDONE}

The present invention relates to a method for preparing N-methyl pyrrolidone, and more particularly, monomethylamine (MMA) aqueous solution and gamma-butyrolactone (GBL) are fed to the reactor to the monomethylamine and gamma-butyro N-methyl pyrrolidone (NMP) produced by the reaction of lactone and water are separated, and the separated water is mixed with monomethylamine to prepare the aqueous monomethylamine solution and introduced into the reactor, N-methyl pyrrolidone It relates to a method for producing (NMP).

N-Methyl pyrrolidone is a low viscosity, colorless, nontoxic, heat resistant organic solvent. It is also a chemically stable, highly polar solvent, making it very useful for many chemical reactions that require inert media. N-methyl pyrrolidone has become more environmentally friendly in areas such as polymer polymerization and processing solvents, paint manufacturing solvents, metal surface cleaners, pharmaceutical synthesis and refining solvents, semiconductor and electronic materials processing solvents, and lithium battery manufacturing solvents. It is a non-toxic product and the demand is increasing.

N-methylpyrrolidone is industrially produced by dehydrating monomethylamine and gamma butyrolactone, which can be classified into two methods, a catalyst-free method and a catalyst-based method.

As a production method without using a catalyst, a method of producing N-methylpyrrolidone with a yield of 90 to 93% by reacting gamma butyrolactone and monomethylamine as raw materials at 280 ° C. for 4 hours in a batch reactor is disclosed. (J. Amer. Chem. Soc., 71 (1949) 896). In addition, Japanese Patent Application Laid-Open No. 1-190667 discloses 94.3% N-methylpyrrolidone by adding gamma butyrolactone, water, and monomethylamine to a high-pressure batch reactor, and reacting at 240 to 265 ° C at 50 atmospheres for 3 hours. One method has been disclosed.

In the production method using a catalyst, a method of preparing N-methylpyrrolidone in a yield of 98% by continuously reacting gammabutyrolactone and monomethylamine under a 280 ° C., atmospheric pressure and a copper ion exchanged Y zeolite catalyst was disclosed. Bull. Chem. Soc. Japan, 50 (10) (1977) 2517). Also disclosed is a process for producing N-methylpyrrolidone from gammabutyrolactone and monomethylamine in a yield of 98.2% by continuous reaction with a chromium ion exchange ZSM-5 zeolite catalyst at 300 ° C. (J. Org. Chem., 50 (1994) 3998). In addition, Japanese Patent Publication No. 49-20582 has a yield of 63-93% of N-methylpyrrolidone from gamma butyrolactone and monomethylamine using a catalyst such as alumina, silica alumina, activated carbon, silica gel, silica magnesia, etc. It discloses a method for producing a. Recently, Akzo Noble has reported in US Pat. No. 5,478,950 the results of continuous reaction at 275 ° C. using a sodium ion exchange X zeolite catalyst to obtain NMP in 96% yield.

However, considering the reduction of the activity of the catalyst in the catalytic reaction method, there are many problems in the long-term use of the catalyst due to frequent catalyst regeneration and separation of the product, and the non-catalytic reaction is effectively judged in terms of economics. Therefore, there is a demand for the development of a new reaction system capable of obtaining a desired product at high yield in a long term without using a catalyst under milder conditions.

Accordingly, the present invention is to improve the problems of the prior art as described above, an object of the present invention is to supply a monomethylamine (MMA) aqueous solution and gamma-butyrolactone (GBL) to the reactor and the monomethylamine and N-methyl pyrrolidone (NMP) produced by the reaction of gamma-butyrolactone and water are separated using a reaction temperature and pressure without additional external heating, and the separated water is mixed with monomethylamine to mix the monomethyl By preparing aqueous amine solution and introducing it into the reactor, the reaction conditions are gentle, the amount of purified water is minimized, and the waste water is reduced, thereby making it possible to economically mass-produce high purity and high yield of N-methyl pyrrolidone (NMP). It provides a method for producing methyl pyrrolidone.

The present invention relates to a method for preparing methyl pyrrolidone, and more particularly, by supplying an aqueous monomethylamine (MMA) solution and gamma-butyrolactone (GBL) to a reactor to react the monomethylamine with gamma-butyrolactone. The resulting N-methyl pyrrolidone (NMP) and water are separated, and the separated water is mixed with monomethylamine to prepare the monomethylamine aqueous solution and introduced into the reactor, thereby obtaining high purity and high yield of N-methyl pyrrolidone. A method for producing N-methyl pyrrolidone capable of mass production of (NMP).

The reaction is sufficiently proceeded at the same time as the optimum reaction conditions in consideration of economy and efficiency, it is preferable to react at a temperature of 260 to 320 ℃ and a pressure of 50 to 120 bar, preferably a temperature of 270 to 310 ℃ and 70 It is preferable to react under pressure of from 110 bar.

In addition, the separated water in the present invention is characterized in that the monomethylamine aqueous solution is recovered and supplied to the reactor by recovering in at least one separator operated at a temperature of 100 to 300 ℃, pressure 0 to 70 bar. When the separated water is circulated through the tube into the reactor, a heater is installed outside the tube to be heated and circulated into the reactor, thereby preventing a change in temperature in the reactor, which may further shorten the reaction time.

In addition, the excess monomethylamine in the reactor is mixed with the separated water and fed to the reactor as an aqueous monomethylamine solution.

The aqueous monomethylamine solution consists of 25 to 65% by weight of monomethylamine (MMA) and 35 to 75% by weight of water, and the monomethylamine (MMA) has a purity of 81 to 100%, and dimethylamine (an impurity) DMA) 0-19% and trimethylamine (TMA) 0-19%.

In the process according to the invention, the molar ratio of gamma-butyrolactone to monomethylamine as starting material is from 1: 1.001 to 1.05, preferably from 1.005 to 1.015.

The gamma-butyrolactone is crude or purified gamma-butyrolactone (GBL), prepared from 1,4-butanediol (BDO). The crude or purified gamma-butyrolactone (GBL) has a purity of 80.000 to 99.999%, and as impurities impurities C3 alcohol, C4 alcohol, tetrahydrofuran, C3 aldehyde, hydroxytetrahydrofuran and 1,4-butanedi It contains at least one selected from the range of 0.001 to 10.000%, and as specific impurities, C3 alcohol 0.001 to 1.000%, C4 alcohol 0.001 to 2.000%, tetrahydrofuran 0.001 to 10.000%, C3 aldehyde 0.001 to 5.000%, hydroxy Tetrahydrofuran 0.001-5.000% and 1,4-butanediol 0.001--10.000%.

In addition, N-methyl pyrrolidone, which is a product obtained after the reaction, is first purified using a distillation apparatus, and then passed through an ion exchange resin to obtain high purity N-methyl blood containing no more than 1 ppb of metal and particles of 0.2 μm or more. Lollidon can be prepared.

The following is more specifically with reference to Figure 1 for the reactor of the present invention.

As shown in FIG. 1, the monomethylamine aqueous solution (F3) and gamma-butyrolactone (F1) were supplied into the reactor R, and then reacted under a reactor internal temperature of 260 to 320 ° C. and a pressure of 50 to 120 bar. The resulting N-methyl pyrrolidone (F4) and water (F4) are separated (S), and the separated water (F6) is recovered in at least one separator operated at a temperature of 100 to 300 ° C. and a pressure of 0 to 70 bar. The mixture is then mixed with monomethylamine (F2) to prepare a monomethylamine aqueous solution (F3) to be circulated back into the reactor (R).

In addition, as shown in Figure 2, after supplying the aqueous monomethylamine solution (F3) and gamma-butyrolactone (F1) in the reactor (R) after the reactor internal temperature of 260 to 320 ℃ and pressure 50 to 120 bar N-methyl pyrrolidone (F4) and water (F4) produced by the reaction are separated (S), and the separated water (F6) is at least one separation operated at a temperature of 100 to 300 ° C and a pressure of 0 to 70 bar. Recovered from the apparatus and mixed with monomethylamine (F2) to prepare a monomethylamine aqueous solution (F3) and circulated back into the reactor (R). N-methyl pyrrolidone (F5) separated in the separator (S) is first purified in a distillator and then passed through an ion exchange resin (F7) to a high purity N-methyl containing no more than 1 ppb of metal and particles of 0.2 μm or more. Prepare pyrrolidone.

Method for preparing N-methyl pyrrolidone according to the present invention is produced by the reaction of the monomethylamine and gamma-butyrolactone by supplying a monomethylamine (MMA) aqueous solution and gamma-butyrolactone (GBL) to the reactor The N-methyl pyrrolidone (NMP) and water were separated, and the separated water was mixed with monomethylamine to prepare the aqueous monomethylamine solution and introduced into the reactor, thereby gently lowering the reaction conditions. Minimize the production efficiency. In addition, by additionally recovering and reusing the water contained in the reaction, it is possible to minimize the amount of wastewater, thereby improving the economics and improving the environmental pollution, thereby dramatically improving the existing production method of N-methyl pyrrolidone (NMP). In addition, when the separated water is circulated through the tube into the reactor, a heater is installed outside the tube to be heated to circulate into the reactor, thereby preventing a change in temperature in the reactor, which may further shorten the reaction time. In addition, the scope of impurities for monomethylamine and gamma-butyrolactone used as raw materials was defined to minimize the production constraints by diversifying the range of raw materials used. The production method of N-methyl pyrrolidone according to the present invention can easily produce the target product in a high yield without a complicated process change in a shorter time than the conventional manufacturing method, and also simplify and yield the process in commercial scale production Can get improvement.

Hereinafter, the present invention will be described in more detail with reference to Examples, but the following Examples are for illustrating the present invention, and the present invention is not limited to the following Examples.

Example 1

Monomethylamine aqueous solution (F3) and gamma-butyrolactone (F1) were supplied to the continuous reactor (R) as a raw material, and then reacted at a liquid space velocity (LHSV) 1.0 under a reactor internal temperature of 300 ° C and pressure of 100 bar. The resulting N-methyl pyrrolidone (F4) and water (F4) were separated (S) at the rear of the reactor, respectively. Separated water (F6) is recovered in one or more separators operating at a temperature of 200 ° C. and a pressure of 40 bar, mixed with monomethylamine (F2) to produce a monomethylamine aqueous solution (F3) and circulated back into reactor (R). I was. The monomethylamine (MMA) was supplied in excess of 1.01 molar ratio with respect to gamma-butyrolactone (GBL), and the conversion and yield according to the concentration of the reactant monomethylamine solution are shown in Table 1 below.

[Comparative Example]

Except that 99.9% monomethylamine gas was used instead of the aqueous monomethylamine solution, the conversion rate and reaction yield to N-methyl pyrrolidone in the same manner as in Example 1 are shown in Table 1 below.

TABLE 1

From Table 1, when the monomethylamine (MMA) is reacted in an aqueous phase rather than a gas phase, it can be seen that the conversion rate and the reaction yield are increased, particularly when the concentration of the monomethylamine (MMA) aqueous solution is 30.6% or 41.9%, respectively. 99.9% conversion and 99.8% or 99.9% reaction yield.

[Example 2]

Experimental results according to the impurities of the monomethylamine as a raw material under the same reaction conditions as in Example 1 are shown in Table 2 below.

TABLE 2

In Table 2, the monomethyl content was lowered to 80%, and even though the impurity dimethylamine or trimethylamine content was increased to 30%, a reaction conversion rate of 99.9% and a reaction yield of 99.7% or more were obtained.

Example 3

Experimental results using the purified gamma butyrolactone and purified gamma butyrolactone under the same reaction conditions as in Example 1 are shown in Table 3 below.

[Table 3]

In Table 3, Experiment 9 is the result of using purified gamma butyrolactone, and Experiments 10 and 11 were prepared without purification of gamma butyrolactone prepared from 1,4-butanediol. 99.9% respectively.

Example 4

The reaction product (F5) prepared under the same reaction conditions as in Example 1 was subjected to ion exchange resin purification device (D) to prepare N-methylpyrrolidone (F7).

 [Table 4]

In Table 4, Experiment 12 was not passed through the ion exchange resin, Experiment 13 was passed through the ion exchange resin to obtain N-methylpyrrolidone. The ion exchange resin was passed through to minimize the metal content and anion content to obtain N-methylpyrrolidone that can be applied for electronic purposes.

1-Process for preparing N-methyl pyrrolidone (R: reactor, S: separator)

Figure 2-Process for preparing N-methyl pyrrolidone (R: reactor, S: separator, D: distillation)

<Description of the code for the drawing code>

F1-gamma-butyrolactone (GBL)

F2-monomethylamine (MMA)

Monomethylamine (MMA) aqueous solution mixed with monomethylamine (MMA) supplied from F3 to F2 and water recovered from F6

F4-Mixture of N-methyl pyrrolidone (NMP) and water

F5-N-methyl pyrrolidone (NMP)

F6-to recover the separated water to prepare a monomethylamine (MMA) aqueous solution of F3

F7-Ion Exchange Resin

Claims (10)

Monomethylamine (MMA) aqueous solution and gamma-butyrolactone (GBL) were fed to the reactor to separate N-methyl pyrrolidone (NMP) and water produced by the reaction of the monomethylamine and gamma-butyrolactone. The separated water is mixed with monomethylamine to prepare the monomethylamine aqueous solution, and introduced into the reactor. The method of claim 1, The reactor internal temperature is 260 to 320 ℃, the pressure is a method for producing N-methyl pyrrolidone, characterized in that 50 to 120 bar. The method of claim 1, The separated water is recovered in at least one separator operated at a temperature of 100 to 300 ℃, pressure 0 to 70 bar to prepare a monomethylamine aqueous solution to supply to the reactor characterized in that the N-methyl pyrrolidone . The method of claim 1, The monomethylamine (MMA) aqueous solution is a method for producing N-methyl pyrrolidone, characterized in that consisting of 25 to 65% by weight of monomethylamine (MMA) and 35 to 75% by weight of water. The method of claim 1, The monomethylamine (MMA) has a purity of 81 to 100%, N-methyl pyrroli characterized in that it contains 0 to 19% dimethylamine (DMA) and 0 to 19% trimethylamine (TMA) as impurities. How to make money. The method of claim 1, The monomethylamine (MMA) is a method for producing N-methyl pyrrolidone, characterized in that it is added in a molar ratio of 1.001 to 1.05 relative to gamma-butyrolactone (GBL). The method of claim 1, The gamma-butyrolactone (GBL) is a crude or purified gamma-butyrolactone (GBL) method for producing N-methyl pyrrolidone. The method of claim 7, wherein The crude or purified gamma-butyrolactone (GBL) is a method for producing N-methyl pyrrolidone, characterized in that prepared from 1,4-butanediol (BDO). The method of claim 8, The crude or purified gamma-butyrolactone (GBL) has a purity of 80.000 to 99.999%, and as impurities impurities C3 alcohol, C4 alcohol, tetrahydrofuran, C3 aldehyde, hydroxytetrahydrofuran and 1,4-butanedi Method for producing N-methyl pyrrolidone, characterized in that it comprises at least one selected from all 0.001 to 10.000%. The method of claim 1, The separated N-methyl pyrrolidone is purified using a distillation apparatus, and a high purity N-methyl pyrrolidone containing no more than 1 ppb of metal and particles of 0.2 μm or more is passed through an ion exchange resin. Method for producing N-methyl pyrrolidone, characterized in that it further comprises.

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