JP2010180199A - Metal complex and method for producing the same - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a metal complex having excellent gas separation performance. <P>SOLUTION: The metal complex comprises a dicarboxylic acid compound (I) represented by general formula (I) (in the formula, R<SP>1</SP>, R<SP>2</SP>and R<SP>3</SP>are each independently hydrogen atom, alkyl which may have substituents, or halogen atom), at least one metal selected from chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc and cadmium, and an organic ligand capable of forming a bidentate ligand with the metal. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

  The present invention relates to a metal complex and a method for producing the same. More specifically, a specific dicarboxylic acid compound, at least one metal selected from chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc and cadmium, and the metal The present invention relates to a metal complex comprising an organic ligand capable of bidentate coordination and a method for producing the same. The metal complex of the present invention is carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, hydrocarbon having 1 to 4 carbon atoms, rare gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor or organic It is preferable as a separating material for separating steam and the like, and particularly preferable as a separating material such as methane and carbon dioxide, hydrogen and carbon dioxide, nitrogen and carbon dioxide.

  So far, various adsorbents have been developed in fields such as deodorization and exhaust gas treatment. Activated carbon is a representative example, and is widely used in various industries such as air purification, desulfurization, denitration, and removal of harmful substances by utilizing the excellent adsorption performance of activated carbon. In recent years, the demand for nitrogen has increased for semiconductor manufacturing processes, etc., and as a method for producing such nitrogen, a method of producing nitrogen from air by pressure swing adsorption method or temperature swing adsorption method using molecular sieve charcoal is used. Has been. Molecular sieve charcoal is also applied to various gas separation and purification such as hydrogen purification from methanol cracked gas.

  When separating mixed gas by pressure swing adsorption method or temperature swing adsorption method, generally, molecular sieve charcoal or zeolite is used as the separation adsorbent, and separation is performed by the difference in the equilibrium adsorption amount or adsorption rate. (For example, refer nonpatent literature 1). However, when separating the mixed gas based on the difference in the amount of equilibrium adsorption, the conventional adsorbents cannot selectively adsorb only the gas to be removed, so the separation factor becomes small and the apparatus must be enlarged. . In addition, when separating the mixed gas based on the difference in adsorption speed, only the gas to be removed can be adsorbed depending on the type of gas, but it is necessary to perform adsorption and desorption alternately, and in this case, the apparatus still has to be large. I didn't get it.

  On the other hand, polymer metal complexes that cause a dynamic structural change by an external stimulus have been developed as adsorbents that give better adsorption performance (see Non-Patent Documents 2 and 3). When this new dynamic structure change polymer metal complex is used as a gas adsorbent, a unique phenomenon is observed in which gas adsorption does not adsorb up to a certain pressure, but gas adsorption starts when a certain pressure is exceeded. Yes. In addition, a phenomenon has been observed in which the adsorption start pressure varies depending on the type of gas.

  When this phenomenon is applied to, for example, an adsorbent in a pressure swing adsorption type gas separation apparatus, very efficient gas separation is possible. Moreover, the time required for the pressure change can be shortened, which contributes to energy saving. Furthermore, since it can contribute to miniaturization of the gas separation device, it is possible to increase cost competitiveness when selling high-purity gas as a product, of course, even when high-purity gas is used inside its own factory Since the cost required for the equipment that requires high purity gas can be reduced, the manufacturing cost of the final product can be reduced.

  Examples of applying the dynamic structure-change polymer metal complex to an occlusion material or separation material include (1) a metal complex having an interdigitated integrated structure (see Patent Document 1), and (2) a two-dimensional lattice stacking type. Metal complexes having an integrated structure (see Patent Document 2, Patent Document 3, Patent Document 4, Patent Document 5, Patent Document 6, and Patent Document 7), (3) Metal complexes having an interpenetrating structure (Patent Document 8) For example).

  However, since any polymer metal complex does not adsorb gas unless it exceeds a certain pressure, it cannot be adsorbed when the partial pressure of the gas to be adsorbed and removed in the mixed gas falls below a certain pressure, so that high purity can be achieved. However, it was difficult to reduce the size of the device.

  A polymer metal complex composed of 2,7-naphthalenedicarboxylic acid, zinc, and 4,4′-bipyridyl shows an I-type adsorption profile in the IUPAC classification, but in a mixed gas adsorption test of carbon dioxide, nitrogen, and oxygen. It is known to selectively adsorb carbon dioxide (see Non-Patent Document 4). However, no mention is made of the effect of the dicarboxylic acid compound on the separation performance in the separation of the mixed gas.

  A polymer metal complex comprising an isophthalic acid derivative, a 2,7-naphthalenedicarboxylic acid derivative, or a 4,4′-benzophenone dicarboxylic acid derivative, a metal ion, and an organic ligand capable of bidentate coordination with the metal ion Has an affinity for unsaturated organic molecules, and is known to be effective for the separation of unsaturated organic molecules (see Patent Document 9). However, no mention is made of the effect of the dicarboxylic acid compound on the separation performance in the separation of the mixed gas.

JP 2004-161675 A JP 2003-275531 A JP 2003-278997 A JP-A-2005-232222 JP 2004-74026 A JP 2005-232033 A JP 2005-232034 A JP 2003-342260 A JP 2008-24784A

Supervised by Atsushi Takeuchi, "The latest adsorption technology handbook" 1st edition, NTS, pages 84-163 (1999) Kazuhiro Uemura, Susumu Kitagawa, Future Materials, Volume 2, 44-51 (2002) Ryotaro Matsuda, Susumu Kitagawa, Peter Tech, 26, 97-104 (2003) Hiroshi Nakagawa, Daisuke Tanaka, Satoru Shimomura, Susumu Kitagawa, 61st Annual Meeting on Colloid and Interface Chemistry, 462 (2008)

  Therefore, an object of the present invention is to provide a metal complex that can be used as a gas separation material that exhibits higher selectivity than conventional ones when the partial pressure of the gas to be adsorbed and removed is low.

  The present inventors have intensively studied, and a specific dicarboxylic acid compound and at least one metal selected from chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc and cadmium. And the present invention found that the above object can be achieved by a metal complex comprising an organic ligand capable of bidentate coordination with the metal.

That is, according to the present invention, the following is provided.
(1) The following general formula (I);

(Wherein R ¹ , R ² and R ³ are the same or different and each represents a hydrogen atom, an alkyl group which may have a substituent or a halogen atom) and a dicarboxylic acid compound (I) represented by At least one metal selected from chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc and cadmium, and an organic ligand capable of bidentate coordination with the metal A metal complex consisting of
(2) An organic ligand capable of bidentate coordination to a metal (hereinafter referred to as “bidentate ligand”) is 1,4-diazabicyclo [2.2.2] octane, pyrazine, 2,5-dimethylpyrazine 4,4′-bipyridyl, 2,2′-dimethyl-4,4′-bipyridine, 1,2-bis (4-pyridyl) ethyne, 1,4-bis (4-pyridyl) butadiyne, 1,4- Bis (4-pyridyl) benzene, 3,6-di (4-pyridyl) -1,2,4,5-tetrazine, 2,2′-bi-1,6-naphthyridine, phenazine, diazapyrene, trans-1, 2-bis (4-pyridyl) ethene, 4,4′-azopyridine, 1,2-bis (4-pyridyl) ethane, 1,2-bis (4-pyridyl) -glycol and N- (4-pyridyl) iso At least one selected from nicotinamide (1 Metal complexes described.
(3) The metal complex according to any one of (1) to (2), wherein the metal is zinc or manganese.
(4) The metal complex according to any one of (1) to (3), wherein the dicarboxylic acid compound is 3,5-pyridinedicarboxylic acid.
(5) A separating material comprising the metal complex according to any one of (1) to (4).
(6) The separator is carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, hydrocarbon having 1 to 4 carbon atoms, rare gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor or The separating material according to (5), which is a separating material for separating organic vapor.
(7) The separation material according to (5), wherein the separation material is a separation material for separating methane and carbon dioxide, hydrogen and carbon dioxide, or nitrogen and carbon dioxide.
(8) From dicarboxylic acid compound (I) and chromium salt, molybdenum salt, tungsten salt, manganese salt, iron salt, ruthenium salt, cobalt salt, rhodium salt, nickel salt, palladium salt, copper salt, zinc salt and cadmium salt A method for producing a metal complex in which at least one selected metal salt and an organic ligand capable of bidentate coordination with the metal are reacted in a solvent and precipitated.

  According to the present invention, a specific dicarboxylic acid compound, at least one metal selected from chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc and cadmium, and A metal complex comprising an organic ligand capable of bidentate coordination can be provided.

  The metal complex of the present invention can be used as a separation material that exhibits high selectivity even when the partial pressure of the gas to be adsorbed and removed is low in the separation of the mixed gas.

3 is a powder X-ray diffraction pattern of the metal complex obtained in Synthesis Example 1. FIG. It is the result of measuring the adsorption-desorption isotherm of carbon dioxide and methane at 273 K by the volumetric method for the metal complex obtained in Synthesis Example 1. 4 is a powder X-ray diffraction pattern of the metal complex obtained in Synthesis Example 2. FIG. It is the result of measuring the adsorption-desorption isotherm of carbon dioxide and methane at 273 K by the volumetric method for the metal complex obtained in Synthesis Example 2. 3 is a powder X-ray diffraction pattern of the metal complex obtained in Comparative Synthesis Example 1. FIG. It is the result of measuring the adsorption / desorption isotherm of carbon dioxide and methane at 273 K by the volumetric method for the metal complex obtained in Comparative Synthesis Example 1.

  The metal complex of the present invention comprises a dicarboxylic acid compound (I) and at least one metal selected from chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc and cadmium. And an organic ligand capable of bidentate coordination with the metal.

  The metal complex of the present invention comprises dicarboxylic acid compound (I), chromium salt, molybdenum salt, tungsten salt, manganese salt, iron salt, ruthenium salt, cobalt salt, rhodium salt, nickel salt, palladium salt, copper salt, zinc salt. And at least one metal salt selected from a cadmium salt and an organic ligand capable of bidentate coordination with the metal are reacted in a solvent under normal pressure for several hours to several days, and are precipitated. be able to. For example, it can be obtained by mixing and reacting an aqueous solution or an organic solution of a metal salt with an organic solution containing an organic ligand capable of bidentate coordination with the dicarboxylic acid compound (I). .

  The dicarboxylic acid compound (I) used in the present invention is represented by the following general formula (I):

It is represented by In the formula, R ¹ , R ² and R ³ are the same or different and each represents a hydrogen atom, an alkyl group which may have a substituent, or a halogen atom.

  The alkyl group preferably has 1 to 5 carbon atoms. Examples of the alkyl group include a straight or branched alkyl group such as a methyl group, an ethyl group, an n-propyl group, an isopropyl group, an n-butyl group, an isobutyl group, a tert-butyl group, and a pentyl group, and a halogen atom. Examples of are fluorine atom, chlorine atom, bromine atom and iodine atom. Examples of the substituent that the alkyl group may have include an alkoxy group (methoxy group, ethoxy group, n-propoxy group, isopropoxy group, n-butoxy group, isobutoxy group, tert-butoxy group, etc. ), Amino group, aldehyde group, epoxy group, acyloxy group (acetoxy group, n-propanoyloxy group, n-butanoyloxy group, pivaloyloxy group, benzoyloxy group, etc.), alkoxycarbonyl group (methoxycarbonyl group, ethoxycarbonyl) Group, n-butoxycarbonyl group, etc.), carboxylic anhydride group (—CO—O—CO—R group) (R is an alkyl group having 1 to 5 carbon atoms) and the like. 1-3 are preferable and, as for the number of the substituents of an alkyl group, one is more preferable.

  As the dicarboxylic acid compound (I), 3,5-pyridinedicarboxylic acid is preferable.

  The mixing ratio of the dicarboxylic acid compound (I) and the bidentate ligand is preferably within a range of a molar ratio of dicarboxylic acid compound (I): bidentate ligand = 1: 5 to 8: 1, and 1: 3 More preferably within the range of a molar ratio of ˜6: 1. Even if the reaction is carried out in a range other than this, the desired metal complex can be obtained, but this is not preferable because the yield is lowered and the side reaction is also increased.

  The mixing ratio of the metal salt and the bidentate ligand is preferably within the range of the molar ratio of metal salt: bidentate ligand = 3: 1 to 1: 3, and the range of the molar ratio of 2: 1 to 1: 2. The inside is more preferable. In other ranges, the yield of the target metal complex decreases, and purification of the metal complex obtained by leaving unreacted raw materials becomes difficult.

  0.01-5.0 mol / L is preferable and, as for the molar concentration of dicarboxylic acid compound (I), 0.05-2.0 mol / L is more preferable. Even if the reaction is performed at a concentration lower than this, the desired metal complex can be obtained, but this is not preferable because the yield decreases. If the concentration is higher than this, the solubility is lowered and the reaction does not proceed smoothly.

  The molar concentration of the bidentate ligand is preferably from 0.01 to 5.0 mol / L, more preferably from 0.05 to 2.0 mol / L. Even if the reaction is performed at a concentration lower than this, the desired metal complex can be obtained, but this is not preferable because the yield decreases. If the concentration is higher than this, the solubility is lowered and the reaction does not proceed smoothly.

  As the metal salt, a metal salt selected from chromium salt, molybdenum salt, tungsten salt, manganese salt, iron salt, ruthenium salt, cobalt salt, rhodium salt, nickel salt, palladium salt, copper salt, zinc salt and cadmium salt is used. Manganese, nickel, copper, zinc, and cadmium salts are preferred. As these metal salts, organic acid salts such as acetates and formates, and inorganic acid salts such as sulfates, nitrates and carbonates can be used. The molar concentration of the metal salt is preferably 0.01 to 5.0 mol / L, more preferably 0.05 to 2.0 mol / L. Even if the reaction is performed at a concentration lower than this, the desired metal complex can be obtained, but this is not preferable because the yield decreases. Further, at a concentration higher than this, unreacted metal salt remains, and purification of the obtained metal complex becomes difficult.

  As the solvent, an organic solvent, water, or a mixed solvent thereof can be used. Specifically, methanol, ethanol, propanol, diethyl ether, dimethoxyethane, tetrahydrofuran, hexane, cyclohexane, heptane, benzene, toluene, methylene chloride, chloroform, acetone, ethyl acetate, acetonitrile, N, N-dimethylformamide, water or These mixed solvents can be used. The reaction temperature is preferably 253 to 423K.

  A metal complex having good crystallinity has high purity and good adsorption performance. The completion of the reaction can be confirmed by quantifying the remaining amount of the raw material by gas chromatography or high performance liquid chromatography. After completion of the reaction, the obtained mixed solution is subjected to suction filtration to collect a precipitate, washed with an organic solvent, and then vacuum dried at about 373 K for several hours to obtain the metal complex of the present invention.

  The metal complex of the present invention obtained as described above forms a two-dimensional sheet in which a one-dimensional chain composed of a dicarboxylic acid compound (I) and a metal ion (for example, zinc ion) is linked by a bidentate ligand. Has been. These two-dimensional sheets are accumulated to form a three-dimensional structure having pores (one-dimensional channels).

  Since the three-dimensional structure in the metal complex of the present invention can be changed in the synthesized crystal, the structure and size of the pores change with the change. That is, by adsorbing a substance, the structure changes to a pore structure having a structurally more stable energy state. The conditions for changing the structure depend on the type of substance to be adsorbed, the adsorption pressure, and the adsorption temperature. That is, in addition to the difference in the interaction between the pore surface and the substance (the strength of the interaction is proportional to the magnitude of the Lennard-Jones potential of the substance), the degree of structural change varies depending on the adsorbed substance, and thus high selectivity To express. In the present invention, the selectivity is further improved by controlling the charge density on the pore surface using a specific dicarboxylic acid compound. In this way, the pores become large, and large molecules are adsorbed in the enlarged pores. After the adsorbed substance is desorbed, it returns to its original structure, so the pore size also returns.

  Although the selective adsorption mechanism is estimated, even if it does not follow the mechanism, it is included in the technical scope of the present invention as long as it satisfies the requirements defined in the present invention.

  Since the metal complex of the present invention can selectively adsorb various gases, carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, hydrocarbons having 1 to 4 carbon atoms (methane, ethane, ethylene, acetylene, etc.) ), Noble gases (such as helium, neon, argon, krypton, xenon), hydrogen sulfide, ammonia, sulfur oxides, nitrogen oxides, siloxanes (such as hexamethylcyclotrisiloxane, octamethylcyclotetrasiloxane), water vapor or organic vapors It is preferable as a separating material for separating the carbon dioxide, particularly suitable for separating carbon dioxide in methane, carbon dioxide in hydrogen, carbon dioxide in nitrogen, etc. by the pressure swing adsorption method or the temperature swing adsorption method. . The organic vapor means a vaporized organic substance that is liquid at normal temperature and pressure. Examples of such organic substances include alcohols such as methanol and ethanol; amines such as trimethylamine; aldehydes such as acetaldehyde; aliphatic hydrocarbons having 5 to 16 carbon atoms; aromatic hydrocarbons such as benzene and toluene; acetone And ketones such as methyl ethyl ketone; halogenated hydrocarbons such as methyl chloride and chloroform.

EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples. Analysis and evaluation in the following examples and comparative examples were performed as follows.

(1) Measurement of powder X-ray diffraction pattern Using an X-ray diffractometer, a range of diffraction angle (2θ) = 5 to 50 ° was scanned at a scanning speed of 1 ° / min, and measured by a symmetric reflection method. Details of the measurement conditions are shown below.
<Analysis conditions>
Apparatus: RINT2400 manufactured by Rigaku Corporation
X-ray source: Cu 40 kV 200 mA
Goniometer: Vertical goniometer Detector: Scintillation counter Step width: 0.02 °
Slit: Divergent slit = 0.5 °
Receiving slit = 0.15mm
Scattering slit = 0.5 °

(2) Measurement of adsorption / desorption isotherm The measurement was performed by a volume method using a high-pressure gas adsorption apparatus. At this time, prior to measurement, 3
Drying was performed at 73K and 50 Pa for 10 hours to remove adsorbed water and the like. Details of the measurement conditions are shown below.
<Analysis conditions>
Apparatus: BELSORP-HP manufactured by Nippon Bell Co., Ltd.
Equilibrium waiting time: 500 seconds

(3) Measurement of mixed gas separation performance A glass 10 mL two-necked flask equipped with a three-way cock and a septum was prepared, and a 100-mL syringe was connected to one of the three-way cocks via another three-way cock with a tube. For measurement, put the sample in a two-necked flask, dry at 373 K, 4.0 × 10 ⁻³ Pa for 3 hours, remove adsorbed water, etc., then close the three-way cock attached to the flask, and then three-way on the syringe side 100 mL of the mixed gas was introduced into the syringe through the cock, and finally, the three-way cock attached to the flask was opened to adsorb the mixed gas to the sample. At this time, the adsorption amount was calculated from the decrease in the scale of the syringe (the dead volume was measured in advance using helium), and the gas composition was calculated by gas chromatography analysis. Details of the measurement conditions are shown below.
<Analysis conditions>
Apparatus: GC-14B manufactured by Shimadzu Corporation
Column: WG-100 manufactured by GL Sciences Inc.
INJ temperature: 100 ° C
DET temperature: 50 ° C
Column temperature: 50 ° C
Carrier gas: helium injection volume: 1 mL
Detector: TCD

Synthesis example 1:
Under a nitrogen atmosphere, 5.00 g (17 mmol) of zinc nitrate hexahydrate, 2.80 g (17 mmol) of 3,5-pyridinedicarboxylic acid and 2.65 g (17 mmol) of 4,4′-bipyridyl were added to N, N-dimethylformamide. Dissolve in 200 mL and stir at 393 K for 24 hours. After suction filtration, it was washed with ethanol three times and dried at 373 K and 50 Pa for 8 hours to obtain 5.17 g (yield 79%) of the target metal complex. The powder X-ray diffraction pattern of the obtained metal complex is shown in FIG. About the obtained metal complex, the result of having measured the adsorption-desorption isotherm of carbon dioxide and methane in 273K by the capacitance method is shown in FIG.

Synthesis example 2
Under a nitrogen atmosphere, manganese nitrate hexahydrate (4.82 g, 17 mmol), 3,5-pyridinedicarboxylic acid (2.80 g, 17 mmol) and 4,4′-bipyridyl (2.65 g, 17 mmol) were added to N, N-dimethylformamide. Dissolve in 200 mL and stir at 393 K for 24 hours. After suction filtration, it was washed 3 times with ethanol and dried at 373 K and 50 Pa for 8 hours to obtain 4.86 g (yield 76%) of the desired metal complex. The powder X-ray diffraction pattern of the obtained metal complex is shown in FIG. About the obtained metal complex, the result of having measured the adsorption-desorption isotherm of carbon dioxide and methane in 273K by the capacitance method is shown in FIG.

Comparative synthesis example 1:
Under a nitrogen atmosphere, 5.00 g (17 mmol) of zinc nitrate hexahydrate, 2.80 g (17 mmol) of isophthalic acid and 2.65 g (17 mmol) of 4,4′-bipyridyl were dissolved in 200 mL of N, N-dimethylformamide, Stir at 393 K for 24 hours. After suction filtration, it was washed with ethanol three times and dried at 373 K and 50 Pa for 8 hours to obtain 6.35 g (yield 98%) of the desired metal complex. FIG. 5 shows a powder X-ray diffraction pattern of the obtained metal complex. About the obtained metal complex, the result of having measured the adsorption-and-desorption isotherm in 273K of a carbon dioxide and methane by the capacitance method is shown in FIG.

Example 1:
For the metal complex obtained in Synthesis Example 1, the separation performance at 273 K and 0.1 MPa was measured using a mixed gas of methane and carbon dioxide having a volume ratio of methane: carbon dioxide = 90: 10. The results are shown in Table 1.

Example 2:
For the metal complex obtained in Synthesis Example 2, the separation performance at 273 K and 0.1 MPa was measured using a mixed gas of methane and carbon dioxide having a volume ratio of methane: carbon dioxide = 90: 10. The results are shown in Table 1.

Comparative Example 1:
For the metal complex obtained in Comparative Synthesis Example 1, the separation performance at 273 K and 0.1 MPa was measured using a mixed gas of methane and carbon dioxide having a volume ratio of methane: carbon dioxide = 90: 10. The results are shown in Table 1.

From Table 1, it is clear that the metal complex of the present invention is excellent as a separator for methane and carbon dioxide because it maintains a high selectivity even when the partial pressure of carbon dioxide is low. Here, "CO ₂ selectivity" is defined as the ratio of carbon dioxide to the total gas adsorbed.

Claims (8)

The following general formula (I);

(Wherein R ¹ , R ² and R ³ are the same or different and each represents a hydrogen atom, an alkyl group which may have a substituent or a halogen atom) and a dicarboxylic acid compound (I) represented by At least one metal selected from chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc and cadmium, and an organic ligand capable of bidentate coordination with the metal A metal complex consisting of   Organic ligands capable of bidentate coordination to metal include 1,4-diazabicyclo [2.2.2] octane, pyrazine, 2,5-dimethylpyrazine, 4,4'-bipyridyl, 2,2'-dimethyl- 4,4′-bipyridine, 1,2-bis (4-pyridyl) ethyne, 1,4-bis (4-pyridyl) butadiyne, 1,4-bis (4-pyridyl) benzene, 3,6-di (4 -Pyridyl) -1,2,4,5-tetrazine, 2,2'-bi-1,6-naphthyridine, phenazine, diazapyrene, trans-1,2-bis (4-pyridyl) ethene, 4,4'- 2. At least one selected from azopyridine, 1,2-bis (4-pyridyl) ethane, 1,2-bis (4-pyridyl) -glycol and N- (4-pyridyl) isonicotinamide. Metal complexes.   The metal complex according to claim 1, wherein the metal is zinc or manganese.   The metal complex according to claim 1, wherein the dicarboxylic acid compound is 3,5-pyridinedicarboxylic acid.   The separating material which consists of a metal complex in any one of Claims 1-4.   The separation material is carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, hydrocarbon having 1 to 4 carbon atoms, rare gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor or organic vapor. The separation material according to claim 5, which is a separation material for separation.   The separation material according to claim 5, wherein the separation material is a separation material for separating methane and carbon dioxide, hydrogen and carbon dioxide, or nitrogen and carbon dioxide.   Dicarboxylic acid compound (I) and selected from chromium salt, molybdenum salt, tungsten salt, manganese salt, iron salt, ruthenium salt, cobalt salt, rhodium salt, nickel salt, palladium salt, copper salt, copper salt, cadmium salt A method for producing a metal complex, wherein at least one metal salt and an organic ligand capable of bidentate coordination with the metal are reacted in a solvent and precipitated.

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