KR20150109607A - Ordered Mesoporous Rhenium-copper-carbon Composite Catalyst, Preparation Method Thereof, and Production Method for 1,4-Butanediol Using Said Catalyst - Google Patents

Abstract

The present invention relates to a method for producing high value-added C4 compounds (γ-Butyrolactone, tetrahydrofuran, and 1,4-butanediol) by applying a noble metal-transition metal-carbon composite catalyst to a hydrogenation reaction of succinic acids and, more specifically, to a method for producing a noble metal-transition metal-carbon composite having a regular mesoporous structure and a method for producing 1,4-butanediol using the catalyst. It is possible to attain a high yield of 1,4-butanediol under a mild condition, if producing 1,4-butanediol by a hydrogenation reaction of succinic acid by means of the catalyst of the present invention.

Description

TECHNICAL FIELD The present invention relates to a rhenium-copper-carbon composite catalyst having a regular mesoporous structure, a method for producing the same, and a production method of 1,4-butanediol using the catalyst. 1,4-Butanediol Using Said Catalyst}

The present invention relates to a process for producing 1,4-butanediol, which is a high-value C4 compound, by applying a noble metal-transition metal-carbon composite catalyst having a regular mesoporous structure to a hydrogenation reaction of succinic acid More particularly, the present invention relates to a noble metal-transition metal-carbon composite catalyst in which the weight ratio of the noble metal to the carbon is 1 wt% to 10 wt% and the weight ratio of the transition metal to the transition metal is 1 wt% to 30 wt% And a process for producing 1,4-butanediol from the hydrogenation reaction of succinic acid using the catalyst.

1,4-butanediol is a chemical widely used in various chemical industries and its market size is continuously increasing. 1,4-butanediol is widely used not only as a raw material for polymer resins such as polybutylene terephthalate (PBT) and polybutylene succinate (PBT) but also as a raw material for high value added materials such as industrial plastics, high elastic fibers, optical films and polyurethane . [J. G. Zeikus, M. K. Jain, P. Elankovan, Appl. Microbiol. Biotechnol., 51, 545 (1999), P. Gallezot, Chem. Soc. Rev., Vol. 41, p. 1538 (2012)]

At present, 1,4-butanediol is used in a high pressure process using formaldehyde and acetylene [US7759531B2], a hydrogenation process of maleic anhydride [US7935834B2], a hydrogenation process of propylene oxide [Z . Xu, B. -H. Guo, Biotechnol. J., 5, 1149 (2010)]. Since 1,4-butanediol is produced using fossil fuel-based reactants, it is vulnerable to supply-demand imbalance due to the rise in international oil prices, and environmental problems such as greenhouse gas emissions are also accompanied. Therefore, a new catalyst process using biomass, an eco-friendly raw material, as a reactant has been greatly appreciated as an alternative process for overcoming such problems is increasing in importance.

Succinic acid is a representative platform compound for the production of petrochemical products and has recently reached a stage where price competition with butane-based maleic anhydride is possible due to the development of the biomass fermentation process. However, the development of a catalyst process capable of efficiently producing C4 compounds (gamma butyrolactone, 1,4-butanediol, and 1,4-butanediol) using succinic acid thus produced has not been developed yet.

Succinic acid is generally converted to C4 compounds (gamma butyrolactone, 1,4-butanediol, and 1,4-butanediol) through hydrogenation at high temperatures and pressures. At this time, 1,4-butanediol having a low-stability chain structure is required to be an active metal having suitable selectivity because it is relatively difficult to manufacture compared with other materials having a cyclic structure. In addition, the carboxylic acid functional group of succinic acid is not used as it may cause side reactions when a catalyst having electrostatic characteristics such as metal oxide is used.

In view of the conversion of succinic acid using various noble metal-supported catalysts, ruthenium, palladium, platinum, rhodium, rhenium [C. Delhomme et al., Green Chem., Vol. 11, p. 13 (2009), I. Bechthold et al., Chem. Eng. Technol., Vol. 31, p. 647 (2008), A. Cukalovic et al., Biofuels Bioprod. Bioref., Vol. 2, p. 505 (2008)]. Carbon-based materials that do not participate in the hydrogenation reaction and do not undergo side reactions are used as the carrier. According to these documents, the hydrogenation reaction of succinic acid shows excellent reaction activity under precious metal catalysts as compared with general transition metal catalysts, but research on two or more kinds of metal complex catalysts for selectively producing specific products is insufficient.

As mentioned above, the 1,4-butanediol production using the conventional noble metal catalyst is a process in which succinic acid is cyclized and converted to gamma butyrolactone and then re-chained again. Therefore, the process proceeds thermodynamically at high temperature and high pressure it's difficult. Therefore, in order to efficiently produce 1,4-butanediol, a new reaction mechanism for selectively hydrogenating only the carbonyl (C = O) group in the carboxylic acid functional group (-COOH) is proposed so that the chain of succinic acid is not cyclized It has emerged as an issue.

Thus, the present inventors introduced a reaction pathway through dimethyl succinate as shown in FIG. 1 using methanol as a solvent. The methylation reaction in which succinic acid is converted to dimethyl succinate by reacting with methanol on a noble metal catalyst takes precedence over the cyclization reaction in which succinic acid is converted to gamma butyrolactone and dimethyl succinate is demethylated on a low cost transition metal catalyst It has an advantage that 1,4-butanediol can be produced under gentle reaction conditions rather than cyclization-reslazed path of succinic acid.

However, existing noble metal supported catalysts prepared for the above reaction path have a disadvantage in that the production process is complicated and the dispersibility and stability of the supported metal are poor. Accordingly, the present inventors have developed a process for preparing a noble metal-transition metal-carbon composite catalyst prepared by one step by injecting both a noble metal precursor and a transition metal precursor in the course of carbon manufacturing by improving the existing surfactant-casting method I aimed to do. In addition, 1,4-butanediol is selectively produced through hydrogenation of succinic acid using the catalyst, thereby achieving higher 1,4-butanediol yield than the conventional reaction system.

US 7759531 B2 US 7935834 B2 KR 1103839 B1 KR 1221557 B1

J. G. Zeikus, M. K. Jain, P. Elankovan, Appl. Microbiol. Biotechnol., 51, 545 (1999). P. Gallezot, Chem. Soc. Rev., vol. 41, p. 1538 (2012). Z. Xu, B. -H. Guo, Biotechnol. J., 5, 1149 (2010). C. Delhomme, D. Weuster-Botz, F. E. K. Hn, Green Chem., Vol. 11, p. I. Bechthold, K. Bretz, S. Kabasci, R. Kopitzky, A. Springer, Chem. Eng. Technol., Vol. 31, p. 647 (2008). A. Cukalovic, C.V. Stevens, Biofuels Bioprod. Bioref., Vol. 2, p. 505 (2008).

Accordingly, an object of the present invention is to provide a noble metal-transition metal-carbon composite having a regular mesoporous structure, which can be easily produced in a single step, maximizing the dispersion of noble metal and transition metal while retaining excellent physico- And to develop high efficiency succinic acid hydrogenation catalyst. Another object of the present invention is to provide a process for producing 1,4-butanediol having a high selectivity by applying the developed noble metal-transition metal-carbon composite catalyst to the hydrogenation reaction of succinic acid.

According to an aspect of the present invention, there is provided a method for producing a noble metal-transition metal-carbon composite in which a noble metal and a transition metal are synthesized by using a surfactant-casting method and each metal is uniformly dispersed.

The manufacturing method includes the following steps

I) dissolving a surfactant, a carbon precursor, a noble metal precursor, a transition metal precursor and a surfactant in an acid solution, and then adding a silica precursor to prepare a carbon / noble metal / transition metal / surfactant / silica complex;

Ii) drying said complex;

Iii) heat-treating the dried carbon / noble metal / transition metal / surfactant / silica complex to completely carbonize the carbon component to obtain a carbon / noble metal / transition metal / silica composite;

And iv) obtaining a noble metal-transition metal-carbon composite catalyst in which a noble metal and a transition metal are uniformly dispersed by removing the silica template from the carbonized carbon / noble metal / transition metal / silica complex.

The drying of step ii) may be performed under an air atmosphere at about 100 ° C, the carbonization in step iii) may be performed in a nitrogen atmosphere at 800 to 1000 ° C, and the removal of the silica template in step iv) .

Wherein the noble metal is at least one selected from the group consisting of rhenium, ruthenium, palladium, platinum and rhodium, and the content of the selected metal is 1 to 10% of the total carbon mass contained in the carbon precursor and the surfactant, Wherein the transition metal is at least one selected from the group consisting of copper, nickel, zinc and tin, and the content of the selected metal is selected from the group consisting of carbon precursor and total carbon And 1 to 30% of the mass.

If the content of the noble metal is less than the above range, the activity of the catalyst is insufficient. If the content of the noble metal exceeds the above range, the aggregation of the metal becomes excessive.

In addition, the present invention is characterized in that the noble metal-transition metal-carbon composite has a pore volume of 0.5 cm ³ / g to 2.0 cm ³ / g and a very large pore volume having a specific surface area of 500 m ² / g to 1800 m ² / And has a specific surface area, and provides a carbon composite catalyst having a regular pore structure.

According to another aspect of the present invention, there is provided a process for preparing succinic acid, which comprises reacting succinic acid in the presence of a porous noble metal-transition metal-carbon composite catalyst at a temperature of from 150 to 250 ° C. and a mild temperature and pressure of from 60 to 100 bar To produce 1,4-butanediol by hydrogenation reaction of succinic acid.

In the present invention, the porous carbon composite material containing noble metal and transition metal prepared by the one-step surfactant-casting method has excellent physical properties such as regular pore structure and high specific surface area of the carbon material itself Therefore, the degree of dispersion of the noble metal and the transition metal is maximized.

In the present invention, when succinic acid is hydrogenated in a liquid phase using the composite catalyst, 1,4-butanediol is produced at a higher yield than a supported catalyst in which a noble metal is supported on a mesoporous carbon support containing a transition metal .

1 shows the reaction mechanism in which succinic acid is converted to 1,4-butanediol via dimethyl succinate.
2 is a graph showing nitrogen adsorption / desorption analysis curves of catalysts containing Re and Cu in the carbon according to the present invention (Re-Cu-MC, Re / Cu-MC, Cu / Re-MC and Re / Cu / MC) .
3 shows the results of a high resolution-transmission electron microscope (HR-NMR) analysis of the catalysts containing Re and Cu in the carbon (Re-Cu-MC, Re / Cu-MC, Cu / Re- TEM) images.
FIG. 4 is a graph showing the relationship between the concentration of succinic acid and the amount of 1,4-butanediol (Re-Cu-MC, Re / Cu-MC, Cu / Re-MC and Re / Cu / MC) ≪ / RTI >

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will now be described in more detail with reference to the accompanying drawings. The present invention relates to a process for preparing a regular mesoporous carbon composite catalyst containing a noble metal and a transition metal, a catalyst prepared by the process, and the production of 1,4 butanediol from succinic acid using the catalyst.

The carbon composite prepared by the one-step surfactant-casting method exhibits excellent physical properties and has an effect of evenly dispersing the noble metal and the transition metal. Therefore, 1,4-butanediol is produced from succinic acid through dimethyl succinate effective. There has been no report on the hydrogenation reaction of succinic acid using the noble metal-transition metal-carbon composite catalyst of the present invention.

The method for producing the noble metal-transition metal-carbon composite having the regular mesoporous structure according to the present invention will be described in more detail as follows. First, an acidic substance such as hydrochloric acid or sulfuric acid, a carbon precursor, a surfactant, a noble metal precursor, and a transition metal precursor are added to distilled water at 40 ° C, and then a silica precursor is gradually added as a template material to prepare a carbon precursor / / Transition metal precursor / surfactant / silica template material.

The carbon precursor is generally used in the art. Generally, a saccharide material (glucose, sucrose) which can be carbonized by dehydration reaction of a hydroxyl group under a high temperature and high pressure is mainly used, and a synthetic catalyst such as sodium carbonate, Cyclic substances (furfuryl alcohol, resorcinol, melamine) which can be dehydrogenated / dehydrated can be used.

The noble metal precursor is not particularly limited, and one or more of the noble metal precursors selected from the group consisting of rhenium, ruthenium, palladium, platinum, and rhodium, which are known to have a reaction activity to hydrogenation of succinic acid, It may be used in a range of 1 to 10% of the total carbon mass contained in the carbon precursor and the surfactant.

Also, the transition metal precursor is not particularly limited, and one or more transition metals selected from the group consisting of copper, nickel, zinc, and tin, which are known to have a reactive activity to the conversion of dimethyl succinate, It may be used in a range of 1 to 30% of the total carbon mass contained in the carbon precursor and the surfactant.

Each precursor is not particularly limited as it is commonly used in the art. The silica precursor is also commonly used in the art and is not particularly limited. The silica precursor may be freely used depending on the solvent, such as TEOS or colloidal silica. The material used as the surfactant is not particularly limited, and any material can be used as long as the pores formed in the carbon composite material obtained after the removal of the silica template and the carbonization of the surfactant can have the mesopores. Preferred examples of the surfactant include F108, F98, F88, P123, P105 and P104, which are pluronic or tetronic block copolymers.

The acid added to the distilled water is a strong acid such as hydrochloric acid, and a strong acid is added in a concentration range of 1 to 5 moles based on the solvent. The amount of the acid used may be an appropriate amount to form the carbon precursor / noble metal precursor / transition metal precursor / surfactant / silica complex within the molar concentration range, and the amount of the acid may be suitably changed depending on the amount of the synthesis catalyst and the carbon precursor .

Next, the solution is sufficiently dried at a temperature of about 100 DEG C for 48 hours, for example. The noble metal / transition metal / carbon / silica composite is calcined by finally heat-treating the fully dried carbon precursor / noble metal precursor / transition metal precursor / surfactant / silica complex under nitrogen atmosphere at 800 to 1000 ° C, To prepare a porous carbon support containing the transition metal from which the silica component has been removed.

Next, the noble metal / transition metal / carbon composite prepared above is reduced with hydrogen gas at 5 to 10% relative to nitrogen at 500 to 700 ° C under a nitrogen atmosphere to finally produce a composite catalyst capable of exhibiting catalytic activity of transition metals and noble metals . At this time, it is preferable to perform the hydrogen treatment at a temperature of 800 ° C or lower, which is the calcination temperature range of the above-mentioned production process, and the accurate temperature can be determined by temperature programmed reduction depending on the kind of the noble metal.

The present invention also provides a process for preparing 1,4-butanediol by subjecting succinic acid to a hydrogenation reaction and a process for producing 1,4-butanediol, wherein hydrogenation is carried out in the presence of the noble metal-transition metal-carbon composite catalyst. The present process is generally carried out in a batch reaction at a suitable temperature and pressure range, and more specifically, at a temperature of 150 to 400 캜 and a pressure range of 30 to 200 bar, but the main process conditions are 300 캜, 100 bar or less It is economically advantageous to carry out the process at a mild temperature and pressure range. Therefore, in the present invention, succinic acid is hydrogenated at a pressure of 200 ° C. and 80 bar. Although the reaction can be carried out at a temperature of 250 ° C. or higher, the chain of succinic acid is thermally decomposed as temperature increases, Setting the appropriate temperature, pressure and time is an important factor that can control the productivity of 1,4-butanediol.

In the present invention, the conversion of succinic acid to 1,4-butanediol is carried out in consideration of the conversion rate in the liquid phase and the volume of the reactor, and since it is a liquid phase process that does not overheat, the catalyst is not easily degraded by carbon deposition, Do. The present catalytic reaction process is a heterogeneous reaction using a solid catalyst by dissolving succinic acid as a reactant in a liquid phase solvent. The solvent is an aromatic substance such as benzene, toluene and xylene, an inert solvent such as dioxane, Methanol may be appropriately mixed and used for conversion to dimethyl succinate. The stirring of the reactor was carried out using a magnetic drive. The agitation speed was generally 300 rpm to 1000 rpm, but in consideration of the state of the catalyst and the viscosity of the solvent, . The amount of the reactant is preferably at least twice the amount of the catalyst, and the specific amount is preferably maintained in a proper ratio in consideration of the maintenance cost, productivity, catalyst regeneration efficiency, and the like in the actual process.

BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in more detail with reference to Preparation Examples and Examples of the present invention.

Manufacturing example  1: Single step ( one - step ) Surfactant - State penal code  Preparation of Rhenium-Copper-Carbon Composite Catalyst

The mesoporous rhenium-copper-carbon composites were fabricated using the surfactant-casting method. First, 450 ml of a 4 molar hydrochloric acid aqueous solution was heated to 40 캜 with stirring, and 14.7 g of a block copolymer surfactant P123 (Aldrich) was dissolved in an aqueous hydrochloric acid solution. 6.1 g of sucrose (Aldrich) and 5.5 ml of aqueous sulfuric acid were added. Then, 5 parts by weight of rhenium and 20 parts by weight of copper precursor were added to the solution, and 27.3 ml of TEOS (Aldrich), which is a silica precursor, was slowly added to the solution, to which a sucrose / rhenium precursor / copper precursor / surfactant / Silica composite was prepared. The complex obtained above was stirred at 40 ° C for 20 hours and then aged at 100 ° C for 24 hours. Then, it is dried in an air atmosphere at 100 ° C for 48 hours and then aged at 160 ° C for 24 hours to obtain a partially carbonized carbon / rhenium / copper / surfactant / silica complex. The partially carbonized composite is finally completely carbonized at a temperature of 800 ° C and a silica mold component is removed with a 5% hydrofluoric acid aqueous solution to prepare a porous carbon support containing rhenium and copper. The mesoporous carbon composite containing rhenium and copper prepared above was reduced to hydrogen gas at 5% of nitrogen at 600 ° C. The prepared catalyst was described as Re-Cu-MC.

Manufacturing example  2: Copper-carbon composite On the carrier  Rhenium Supported  Catalyst preparation

A mesoporous carbon support (Cu-MC) containing only copper was prepared in the same manner as in Preparation Example 1, except that the rhenium precursor was not used. Then, rhenium was supported on the carbon support to prepare a rhenium-supported catalyst. First, the precursor of rhenium metal, rhenium chloride, is dissolved in acetone. At this time, the amount of acetone was kept at 0.1 ml per 1 g of the catalyst in the minimum amount. The thus-prepared solution was impregnated with a rhenium: Cu-MC carrier in a weight ratio of 0.05: 1, and a physical force was applied thereto. At this time, the carbon carrier was adjusted so as to be moistly wetted by adding the acetone very little (incipient wetness method). Thereafter, the impregnated rhenium-supported catalyst was dried at 40 DEG C to remove all the acetone, and then calcined at 600 DEG C for 4 hours under a nitrogen atmosphere. The rhenium-supported catalyst prepared above was reduced to 5% hydrogen gas at 600 ° C in terms of nitrogen, and was described as Re / Cu-MC.

Manufacturing example  3: rhenium-carbon composite On the carrier  Copper Supported  Catalyst preparation

A mesoporous carbon support (Re-MC) containing only rhenium was prepared in the same manner as in Preparation Example 1, except that the copper precursor was not used. Then, copper was supported on the carbon support to prepare a copper-supported catalyst. First, copper nitrate, a precursor of copper metal, is dissolved in acetone. At this time, the amount of acetone was kept at 0.1 ml per 1 g of the catalyst in the minimum amount. The thus prepared solution was put into a carrier so that the weight ratio of copper: Cu-MC carrier was 0.2: 1, and impregnated with the initial wetting technique of Production Example 2 above. Subsequently, the impregnated copper-supported catalyst sample was dried at 40 DEG C to remove all the acetone, and then the catalyst was calcined at 600 DEG C for 4 hours under a nitrogen atmosphere. The copper-supported catalyst prepared above was reduced to hydrogen gas at 5% of nitrogen at 600 ° C and was described as Cu / Re-MC.

Manufacturing example  4: Carbon On the carrier  Rhenium and copper Supported  Catalyst preparation

A carbon carrier (MC) was prepared in the same manner as in Preparation Example 1, except that the rhenium precursor and the copper precursor were not used. Then, rhenium and copper were supported on the carbon support to prepare rhenium and copper supported catalysts. First, copper nitrate, a precursor of copper metal, is dissolved in acetone. At this time, the amount of acetone was kept at 0.1 ml per 1 g of the catalyst in the minimum amount. A carrier was added to the thus-prepared solution so that the weight ratio of the copper: MC carrier was 0.2: 1, and impregnated with the initial wetting technique of Production Example 2 above. Subsequently, the impregnated copper-supported catalyst sample was dried at 40 DEG C to remove all the acetone, and then the catalyst was calcined at 600 DEG C for 4 hours under a nitrogen atmosphere. Then, an acetone solution in which rhenium chloride, which is a precursor of rhenium metal, was dissolved was impregnated into a carrier so that the weight ratio of rhenium: MC carrier was 0.05: 1, and impregnated in the same manner as above. Thereafter, the impregnated rhenium and copper supported catalyst samples were dried at 40 DEG C to remove all the acetone, and then the catalyst was calcined at 600 DEG C for 4 hours under a nitrogen atmosphere. The rhenium and copper supported catalysts prepared above were reduced to 5% hydrogen gas at 600 < 0 > C relative to nitrogen and were reported as Re / Cu / MC.

Example  1 and Comparative Example  1: Catalyst containing rhenium and copper in carbon ( Re - Cu - MC , Re / Cu-MC, Cu / Re - MC , Re / Cu / MC Analysis and comparison of characteristics

Table 1 shows the results of nitrogen adsorption and desorption experiments of Re-Cu-MC, Re / Cu-MC, Cu / Re-MC and Re / Cu / MC catalysts prepared by the above- The nitrogen adsorption / desorption curve is shown in Fig.

Specific surface area
(m ² / g) Pore volume
( cm ³ / g) Pore size
( nm ) Metal dispersion degree
(%) MC 1189 1.18 4.3 - Re - Cu - MC 1169 1.04 3.6 17.9 Re / Cu - MC 898 0.86 3.8 8.4 Cu / Re - MC 624 0.64 4.1 4.5 Re / Cu / MC 555 0.62 4.4 3.6

As shown in Table 1, it can be seen that the specific surface area and the pore volume gradually decrease as the number of the carriers is increased. This is due to the phenomenon that the metals that are carried on the back due to the repeated deposition cause clogging of the pores of the carbon carrier can see. In addition, the pore size tended to decrease as the metal prepared in a single step including the carbon material increased. This is because the thickness of the silica wall was small as the metal precursor was present at the carbon / silica interface in the process of preparing the catalyst It is seen as a phenomenon that occurs because of the loss.

As can be seen from the above table, Re-Cu-MC composite catalyst has the most excellent surface properties close to the carbon support. In addition, when the metal surface area of the catalyst measured by the carbon monoxide adsorption experiment is examined, the metal dispersion degree of the Re-Cu-MC composite catalyst having the best surface characteristics is the largest.

Transmission electron microscopy (HR-TEM) was used to determine the surface morphology of the Re-Cu-MC, Re / Cu-MC, Cu / Re-MC and Re / Cu / , Which is shown in Fig. When the transmission electron microscope images shown in FIG. 3 are compared, it is possible to observe a change in the surface depending on the production form of rhenium and copper. Compared with the carbon carrier MC prepared in Preparation Example 4, the carbon structure of all the catalysts maintained a regular pore shape well. It can be seen that the particle size is small and uniformly dispersed as the number of metals produced in a single step increases. However, as the number of deposition was increased, the dispersion of metal particles decreased significantly due to agglomeration. Therefore, based on the results of Table 1 and FIG. 3, it can be seen that the dispersity of Re-Cu-MC composite catalyst prepared with a single step of rhenium and copper is the best.

Example  2 and Comparative Example  2: Catalyst containing carbon and rhenium ( Re - Cu - MC , Re / Cu-MC, Cu / Re - MC , Re / Cu / MC ) By hydrogenation of succinic acid in 1,4- Butanediol  production

The hydrogenation reaction of succinic acid was carried out using catalysts (Re-Cu-MC, Re / Cu-MC, Cu / Re-MC and Re / Cu / MC) The reaction results are shown in Table 2 and FIG. 4.

Suche mountain
Conversion Rate (%) Dimethyl succinate   Yield (%) gamma Butyrolactone
Yield (%) 1,4- Butanediol
Yield (%) Re - Cu - MC 100 53.1 20.3 17.2 Re / Cu - MC 100 53.6 19.5 15.0 Cu / Re - MC 100 60.5 19.3 12.1 Re / Cu / MC 100 66.3 14.6 6.7

The conversion of succinic acid was carried out in a liquid phase reaction, using a batch reactor. To the reaction, 0.2 g of catalyst and 0.5 g of succinic acid were charged in an autoclave reactor together with a mixture of 25 ml of 1,4-dioxane solvent and 25 ml of methanol, It removes all oxygen inside. Subsequently, hydrogen is injected and heated to a reaction temperature at a heating rate of 10 ° C / min when a pressure of about 40 bar is reached. When the reaction temperature is reached, the pressure is increased to 80 bar by using hydrogen again, and this time is defined as the reaction start time. The total reaction time was 20 hours, and the stirring rate was performed at 700 rpm, which is the maximum mass transfer rate. After the reaction was completed, the temperature was cooled to room temperature, the pressure was removed, and the catalyst and the liquid product were separated by filtration and analyzed by gas chromatography (GC). The product was a hydrogenation product, an intermediate dimethyl succinate, a target product 1,4-butanediol, and a by-product gamma butyrolactone.

(Re-Cu-MC, Re / Cu-MC, Cu / Re-MC and Re / Cu / MC) containing copper and copper in the carbon containing copper according to the present invention The conversion rate was 100%. This means that the catalysis of rhenium in which the methylation of succinic acid occurs takes place well in all catalysts. On the other hand, the conversion of dimethyl succinate to 1,4-butanediol, which is associated with the catalytic action of copper, increased as the degree of dispersion of copper increased, due to active demethylation. However, it can be seen that the 1,4-butanediol yield decreases as the dispersion degree decreases as the number of the supports increases. Therefore, in the present invention, Re-Cu-MC composite catalyst having the most excellent surface properties and metal dispersibility is the most efficient catalyst for producing 1,4-butanediol.

The embodiments of the present invention described above should not be construed as limiting the technical idea of the present invention. The scope of protection of the present invention is limited only by the matters described in the claims, and those skilled in the art will be able to modify the technical idea of the present invention in various forms. Accordingly, such improvements and modifications will fall within the scope of the present invention as long as they are obvious to those skilled in the art.

Claims (6)

As a method for producing a mesoporous noble metal-transition metal-carbon composite catalyst for producing 1,4-butanediol from succinic acid through dimethyl succinate
I) dissolving a surfactant, a carbon precursor, a noble metal precursor, a transition metal precursor and a surfactant in an acid solution, and then adding a silica precursor to prepare a carbon / noble metal / transition metal / surfactant / silica complex;
Ii) drying the composite under an air atmosphere;
Iii) subjecting the dried carbon / noble metal / transition metal / surfactant / silica complex to heat treatment at 800 to 1000 ° C under a nitrogen atmosphere to completely carbonize the carbon component to obtain a carbon / noble metal / transition metal / silica composite;
And iv) obtaining a noble metal-transition metal-carbon composite catalyst in which noble metal and transition metal are evenly dispersed by removing silica from the carbonized carbon / noble metal / transition metal / silica composite. Gt; The method of claim 1, wherein the noble metal is at least one selected from the group consisting of rhenium, ruthenium, palladium, platinum, rhodium, and the content of the selected metal is selected from the group consisting of carbon precursor and total carbon By weight of the total weight of the composite catalyst. The method of claim 1, wherein the transition metal is at least one selected from the group consisting of copper, nickel, zinc, and tin, and the content of the selected metal is selected from the group consisting of carbon precursor and total carbon mass ≪ / RTI > by weight of the composite catalyst. The method of claim 1, wherein the noble metal is rhenium, and the transition metal is copper. A noble metal-transition metal-carbon composite catalyst produced by the method of any one of claims 1 to 4, wherein the catalyst has a pore volume of 0.5 cm ³ / g to 2.0 cm ³ / g and a specific surface area of 500 m ² / g to 1800 m < ² > / g, and a specific surface area. Characterized in that 1,4-butanediol is produced from succinic acid through dimethyl succinate by using the catalyst of claim 5 at a temperature of 150 ° C to 400 ° C and a pressure range of 30 to 200 bar.

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